WO2006121361A1 - Process for the preparation of gelatine and gelatine hydrolyzate - Google Patents

Process for the preparation of gelatine and gelatine hydrolyzate Download PDF

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Publication number
WO2006121361A1
WO2006121361A1 PCT/PL2006/000028 PL2006000028W WO2006121361A1 WO 2006121361 A1 WO2006121361 A1 WO 2006121361A1 PL 2006000028 W PL2006000028 W PL 2006000028W WO 2006121361 A1 WO2006121361 A1 WO 2006121361A1
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WIPO (PCT)
Prior art keywords
gelatine
maceration
water
reactor
acid
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PCT/PL2006/000028
Other languages
French (fr)
Inventor
Halina Grabek
Kazimierz Grabek
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Halina Grabek
Kazimierz Grabek
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Filing date
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Application filed by Halina Grabek, Kazimierz Grabek filed Critical Halina Grabek
Publication of WO2006121361A1 publication Critical patent/WO2006121361A1/en

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    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09H—PREPARATION OF GLUE OR GELATINE
    • C09H3/00—Isolation of glue or gelatine from raw materials, e.g. by extracting, by heating
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09H—PREPARATION OF GLUE OR GELATINE
    • C09H3/00—Isolation of glue or gelatine from raw materials, e.g. by extracting, by heating
    • C09H3/02—Purification of solutions of gelatine

Definitions

  • This invention relates to the process for the preparation of the gelatine and the gelatine hydrolyzate from animal bones .
  • the gelatine and its hydrolyzate are the animal protein which do not occur in the nature but they are produced by the chemical-thermic methods from the collagen.
  • the raw material for the production of the gelatine and the gelatine hydrolyzate is the collagen which is present in the skin, bones and other kinds of the connective tissue.
  • the collagen has a very complicated and outspread protein structure which undergoes partial reduction during the process of the gelatine production, which consequently leads to the changes of its characteristic physical and chemical properties.
  • the production of the gelatine from animal bones is a very complicated process.
  • the first stage of this process is the appropriate preparation of the bone raw material.
  • the bones which are the waste product from the slaughter of the animals, after the cutting off the meat and the preliminary classification, are crumbled to the bone shot and the defatting is carried out with the hot water or the steam.
  • the dried and defatted bone shot is subjected to the process of demineralization - maceration by traeting it for several to a dozen or so days with the hydrochloric acid diluted to a few percents.
  • the bone raw material cleaned in such a way and called the ossein is used for the production of the gelatine.
  • the by-product precipitated from the acidic bone extract and containing calcium salt is used among others as the component of the fodder feeding stuffes .
  • the ossein prepared by the acidic method is then subjected to the multi-stage extraction with the hot water and increasing temperature of the process in the subsequent extraction operations.
  • First fractions obtained at the lowest temperature give gels of the highest quality.
  • the material which remains after the first extraction is subjected to the next extraction with the fresh water of a higher temperature. This process is repeated until all the remaining gelatine is transfered to the solution.
  • the gelatine solution obtained after the extraction is next cleaned off the traces of the fat and fibrils derived from the raw material with the use of different known methods, e.g. highly efficient centrifuges and filters.
  • the subsequent stages of the process consist of concentrating, cooling, drying, milling, mixing of the gelatine and preparation for ready use.
  • the gelatine hydrolyzates are usually produced from the cattle and swine skin.
  • the alkaline molecules of the collagen are decomposed by the proteolytic enzymes to the polypeptides mixture of a different chain length.
  • the obtained liquid hydrolyzate is then sterilized, concentrated and dried.
  • the volume of the liquid wastes formed in this stage is also very big and results in large costs connected with the environment protection against the negative effects.
  • the defatting process is carried out in a high temperature which involves a high consumption of the electric and thermal energy required to heat the reactor content and maintain it in a high temperature.
  • the electric and thermal energy is also consumed in the process of drying the product in ' a very high temperature and the subsequent classification of the bone shot.
  • the method of the gelatine production from different kinds of the raw material containing the collagen is known from the international patent application Nr WO9421739.
  • the raw material is milled into the particles of the size not exceeding 1 mm and the milled raw material is mixed with water in order to obtain the suspension.
  • the acid is added to the suspension to set pH on the level from 2 to 5 and the suspension is heated to the temperature of 60-1300 0 C at the time from 1 second to 1 hour.
  • the base is added to the suspension in order to rise pH value and the suspension is separated onto the liquid phase containing the gelatine and the solid phase, and then the gelatine is recovered from the liquid phase via filtration and cleaning.
  • the preliminary stage may be the defatting of the raw material to the content of the fat on the level of about 3%. It is indicated that this stage is not necessary but it should be taken into account that the method of this application is used for different kinds of the raw material and also for the raw material of a small content of the fat (e.g. oxen skin), and in such a case the defatting may be indeed useless.
  • the analysis of the description and especially of the examples enables the statement that in the case of the use of animal bones as the raw material containing the collagen, the preliminary stage of the defatting is carried out with the technology and the suitable equipment of Alfa Laval Centribone.
  • the maceration stage is carried out in a high temperature.
  • the reaction rate significantly rises and by the same rises the decomposition rate of the organic material.
  • the necessity of milling the raw material to very small particles and adding a large quantity of water to them as well as carrying out the maceration in a high temperature is connected with a high energy consumption.
  • the subject of the invention is to provide such a process for the preparation of the gelatine and its hydrolyzate which eliminates the problems connected with the preliminary defatting of the raw material in the form of the crumbled bones and especially the process which reduces the volume of the liquid wastes harmful for the environment and also lowers the level of the electric and thermal energy consumption.
  • the process of the invention for the preparation of the gelatine and its hydrolyzate consists in that the crumbled animal bones are subjected to the maceration process with the acid of the concentration not higher than 34% at the time from 1 to 14 days, and during the maceration or after its termination, the calcium salts are separated from the post-maceration lyes and the ossein obtained in this way, after the remaining acid is removed, preferably by rinsing with water, possibly containing the alkaline substance, is subjected to at least once extraction with the water at the temperature from 40 to 1200 0 C.
  • the water extract of the gelatine is cleaned by the use of the known methods, the extract is concentrated, possibly dried and milled, and in order to obtain the gelatine hydrolyzate, to the water extract there is added the proteolytic enzym which is later inactivated, and the extract is cleaned by the use of the known methods, concentrated and dried.
  • the process of the invention is characterized in that the fat is removed from the reaction environment at the time of the maceration process and/or the extraction and/or after the termination of the maceration process and/or the extraction, by the separation of the water phase and the fatty phase or, in the case when the fat is removed after the termination of the extraction process, by the separation of the water phase containing the gelatine, the fatty phase and the solid phase or by the separation of the water phase containing the gelatine from the fatty phase combined with the solid phase.
  • the separation of the fatty phase and the water phase is carried out by the continuous or batch method.
  • hydrochloric acid is used as the acid.
  • the bones Before the stage of the maceration, the bones may be subjected to the proces of the muscle removal.
  • the crumbled and possibly free of muscles animal bones are rinsed out with water.
  • the process for the maceration is carried out with or without mixing of the reactor content.
  • the acid for the maceration process is delivered to the reactor from its bottom and/or from its side, and the post-maceration lyes are collected from the top of the reactor.
  • the acid for the maceration process is delivered from the top of the reactor, and the post- maceration lyes are collected from the bottom and/or from the side of the reactor.
  • the acid for the maceration process is delivered from the side of the reactor, and the post- maceration lyes are collected from the top and/or from the bottom and/or from the side of the reactor.
  • bones are classified by the kind of the animal species and/or the kind of the bones.
  • the proteolytic enzym is added in the quantity of at least 0,01% in relation to the dry mass of the gelatine present in the extract.
  • the proteolytic enzym is inactivated by rising the temperature of the extract containing the gelatine.
  • the substance of the invention is the removal of the fat at the stage and/or after the stage of the extraction and/or the maceration, but not, as in the known processes, before the bone raw material is subjected to maceration with the acid.
  • the change of the defatting stage to the phase of the maceration and/or extraction enables the significant reduction of the volume of the liquid wastes formed in process. It happens thanks to the elimination of a large quantity of water introduced according to the process of the invention in which the whole first stage of the process for the preparation of the gelatine, namely the production of the defatted bone shot, is omitted.
  • the bone material received from the meat processing plants and other sources should be only crumbled and then, without the preliminary defatting and without drying, is transfered to the production of the gelatine. Possibly, the bones are subjected to the process of the muscles removal if this process has not been earlier carried out in the meat processing plant.
  • the whole module of the machines and devices for the preparation of the defatted bone shot and the installations and the production areas connected with them are eliminated. It leads to very big savings of the electric and thermal energy and a significant reduction of the costs connected with processing of the liquid wastes containing some quantities of the fat and proteins as well as a significant reduction of the costs for the preparation of the final product.
  • the fat removed at the extraction stage contains water in a much lower quantity and thanks to that the fat separation may be much more easier and cheaper.
  • the fat may be later used as the raw material in different applications, among others in the chemical industry.
  • the pork bones from the meat processing plants and other sources along with the remaining meat tissue are crumbled onto pieces of the size from 1 to 10 mm and rinsed out with cold water in order to remove the remainder of the blood.
  • the crumbled bones are introduced to the reactor and flooded repeatedly with hydrochloric acid of the concentration of 3,8% at the volume ratio of the bones to the acid solution of 1:2,27 until the macerated bones is obtained.
  • the calcium salts are separated from the post-maceration lyes by precipitation.
  • the ossein produced is washed with water in order to remove the acid until pH not ecxeeding 5 is obtained.
  • the ossein is flooded with water in the quantity of no more than 5 volumes of the ossein and heated to the temperature of 50 0 C.
  • the extraction process is carried out several times until the gelatine is transfered from the ossein to the water solution, and next the gelatine solution in the water is collected from the reactor.
  • the fatty phase is periodicaly removed by pumping out from the upper part of the reactor.
  • the water phase with the gelatine is transfered from the reactor to the tanks, and next it is cleaned, deionized, possibly by the ultrafiltration.
  • the residue after the extraction process is withdrawn from the reactor in order to separate the remaining fat, the gelatine solution and solid parts.
  • the gelatine obtained has the gel hardness of 253 bloom.
  • the pork bones from the meat processing plants and other sources along with the remaining meat tissue are crumbled onto pieces of the size from 1 to 10 mm.
  • the crumbled bones are introduced to the reactor and flooded repeatedly with hydrochloric acid of the concentration of 4,2% at the volume ratio of the bones to the acid solution of 1:2,5 until the macerated bones are obtained.
  • the calcium salts are separated from the post- maceration lyes by precipitation.
  • the ossein produced is washed with water in order to remove the acid until pH not ecxeeding 5 is obtained.
  • the ossein is flooded with water in the quantity of no more than 5 volumes of the ossein and heated to the temperature of 55°C.
  • the extraction process is carried out several times until the gelatine is transfered from the ossein to the water solution, and next the gelatine solution in the water is collected from the reactor.
  • the residue present in the reactor is transfered to a separate tank in which the preliminary collection of the fat is carried out by pumping out.
  • the residue is transfered to the decanter where the remainig fat, the water phase containing the gelatine and the solid phase are separated.
  • the water phases containing the gelatine from the extraction stage and collected from the decanter are cleaned and deionized, possibly by ultrafiltration.
  • the subsequent stages include concentration on the evaporators, cooling, drying, milling, mixing and packing of the final product.
  • the gelatine obtained has the gel hardness of 302 bloom.
  • the ossein produced is washed with water with the addition of the base in order to remove the acid until pH not ecxeeding 5 is obtained.
  • the ossein is flooded with water in the quantity of no more than 5 volumes of the ossein and heated to the temperature of 99°C.
  • the extraction process is carried out several times increasing the temperature until the gelatine from the ossein is transfered to the water solution, and next the gelatine solution in the water is collected from the reactor.
  • the fatty phase is periodicaly removed by pumping out from the upper part of the reactor.
  • the water phase with the gelatine is transfered from the reactor to the tanks.
  • the residue after the extraction process is withdrawn from the reactor in order to separate the remaining fat, the gelatine solution and solid parts.
  • the water phases containing the gelatine are cleaned, deionized, possibly by ultrafiltration, and concentrated on the evaporators, cooled, dried, milled, mixed and packed as the final product.
  • the gelatine obtained has the gel hardness of 248 bloom.
  • the pork bones from the meat processing plants and other sources along with the remaining meat tissue are crumbled onto pieces of the size from 1 to 10 mm.
  • the crumbled bones are introduced to the reactor and flooded repeatedly with hydrochloric acid of the concentration of 4,2% at the volume ratio of the bones to the acid solution of 1:2,5 until the macerated bones are obtained.
  • the calcium salts are separated from the post- maceration lyes by precipitation.
  • the ossein produced is washed with water in order to remove the acid until pH not ecxeeding 5,1 is obtained.
  • the ossein is flooded with water in the quantity of no more than 5 volumes of the ossein and heated to the temperature of 58°C.
  • the extraction process is carried out several times until the gelatine is transfered from the ossein to the water solution, and next the gelatine solution in the water is collected from the reactor.
  • the residue present in the reactor is transfered to the separate tank in which the preliminary collection of the fat is carried out by pumping out. Then, the residue is transfered to the decanter where the remainig fat, the water phase containing the gelatine and the solid phase are separated.
  • the base in order to increase pH to 7,5 and then the proteolytic enzym Bacillus amyloliquefacies (Mulitfect P-3000) is added in the quantity of 0,5% in relation to the dry mass of the gelatine present in the water phase.
  • the base and enzym are added with the continuous mixing of the reactor content. After 1 hour, the temperature of the extract is increased to 80 0 C in order to inactivate the enzym and then the extract is cleaned, concentrated and spray-dried.

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  • Organic Chemistry (AREA)
  • Meat, Egg Or Seafood Products (AREA)
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Abstract

The process of the invention for the preparation of the gelatine consists in that the crumbled animal bones are subjected to the maceration process with the acid of the concentration of not higher than 34% at the time from 1 to 14 days, during the maceration or after its termination from the post-maceration lyes the calcium salts are sepatated, and the ossein produced in this way, after the remainder of the acid is removed, possibly with the addition of the alkaline substance, is subjected to at least once extraction with water of the temperature from 40 to 1200°C, possibly in the case of the production of the gelatine hydrolyzate, to the water extract of the gelatine the proteolytic enzym is added and next it is inactivated, then the water extract of the gelatine or the gelatine hydrolyzate is cleaned using the known methods, the extract is concentrated, possibly dried and milled. The process of the invention is characterized in that the fat is removed from the reaction environment at the time of the maceration process and/or the extraction and/or after the termination of the maceration process and/or the extraction by the separation of the water phase containing the gelatine and the fatty phase and possibly the solid phase.

Description

Process for the preparation of gelatine and gelatine hydrolyzate
This invention relates to the process for the preparation of the gelatine and the gelatine hydrolyzate from animal bones .
The gelatine and its hydrolyzate are the animal protein which do not occur in the nature but they are produced by the chemical-thermic methods from the collagen. The raw material for the production of the gelatine and the gelatine hydrolyzate is the collagen which is present in the skin, bones and other kinds of the connective tissue. The collagen has a very complicated and outspread protein structure which undergoes partial reduction during the process of the gelatine production, which consequently leads to the changes of its characteristic physical and chemical properties.
The production of the gelatine from animal bones is a very complicated process. The first stage of this process is the appropriate preparation of the bone raw material. In this stage, the bones which are the waste product from the slaughter of the animals, after the cutting off the meat and the preliminary classification, are crumbled to the bone shot and the defatting is carried out with the hot water or the steam. The dried and defatted bone shot is subjected to the process of demineralization - maceration by traeting it for several to a dozen or so days with the hydrochloric acid diluted to a few percents. The bone raw material cleaned in such a way and called the ossein is used for the production of the gelatine. The by-product precipitated from the acidic bone extract and containing calcium salt is used among others as the component of the fodder feeding stuffes .
The ossein prepared by the acidic method is then subjected to the multi-stage extraction with the hot water and increasing temperature of the process in the subsequent extraction operations. First fractions obtained at the lowest temperature give gels of the highest quality. The material which remains after the first extraction is subjected to the next extraction with the fresh water of a higher temperature. This process is repeated until all the remaining gelatine is transfered to the solution. The gelatine solution obtained after the extraction is next cleaned off the traces of the fat and fibrils derived from the raw material with the use of different known methods, e.g. highly efficient centrifuges and filters. The subsequent stages of the process consist of concentrating, cooling, drying, milling, mixing of the gelatine and preparation for ready use.
The gelatine hydrolyzates are usually produced from the cattle and swine skin. As a result of the longterm maceration, the alkaline molecules of the collagen are decomposed by the proteolytic enzymes to the polypeptides mixture of a different chain length. The obtained liquid hydrolyzate is then sterilized, concentrated and dried.
Many technological problems are connected with the first stage of the preparation of the raw material for the production of the gelatine in which the bone shot is produced and especially with the stage of defatting the bone raw material. In the defatting process of the bone raw material, prior to the maceration, it is necessary to introduce to the raw material a big quantity of water of a very high temperature and next to drain this water along with the washed out fat. In the defatting process of the raw material, there is removed about 70% of the fat delivered together with the bones in the form of the water-fat emulsion constituting the post-operation residue which creates difficulties in the subsequent processing and produces a big quantity of the liquid wastes . Due to the fact that a large volume of the water is introduced to the raw material, the volume of the liquid wastes formed in this stage is also very big and results in large costs connected with the environment protection against the negative effects. In an overall process, it is also important that the defatting process is carried out in a high temperature which involves a high consumption of the electric and thermal energy required to heat the reactor content and maintain it in a high temperature. The electric and thermal energy is also consumed in the process of drying the product in 'a very high temperature and the subsequent classification of the bone shot.
The method of the gelatine production from different kinds of the raw material containing the collagen is known from the international patent application Nr WO9421739. According to the method of this application, the raw material is milled into the particles of the size not exceeding 1 mm and the milled raw material is mixed with water in order to obtain the suspension. The acid is added to the suspension to set pH on the level from 2 to 5 and the suspension is heated to the temperature of 60-13000C at the time from 1 second to 1 hour. In the next stage, the base is added to the suspension in order to rise pH value and the suspension is separated onto the liquid phase containing the gelatine and the solid phase, and then the gelatine is recovered from the liquid phase via filtration and cleaning. In the method of the invention, the preliminary stage may be the defatting of the raw material to the content of the fat on the level of about 3%. It is indicated that this stage is not necessary but it should be taken into account that the method of this application is used for different kinds of the raw material and also for the raw material of a small content of the fat (e.g. oxen skin), and in such a case the defatting may be indeed useless. The analysis of the description and especially of the examples enables the statement that in the case of the use of animal bones as the raw material containing the collagen, the preliminary stage of the defatting is carried out with the technology and the suitable equipment of Alfa Laval Centribone.
According to the method of the application Nr WO9421739, the maceration stage is carried out in a high temperature. Although it is possible to shorten the time of this gelatine production process, in a high temperature the reaction rate significantly rises and by the same rises the decomposition rate of the organic material. In such circumstances, it is very difficult to set the time of the maceration necessary to obtain the gelatine of the assumed quality in the later part of the process. Moreover, the necessity of milling the raw material to very small particles and adding a large quantity of water to them as well as carrying out the maceration in a high temperature is connected with a high energy consumption. In the case of the use of animal bones as the raw material, the process of the application Nr WO9421739 undoubtedly comprises the preliminary defatting stage. It results from the fact that both in the schematic presentation of the process stages and in the invention description there is no information about the removal of the bone fat introduced in any other stage than the preliminary one and the fat must certainly be removed from the reaction environment.
The subject of the invention is to provide such a process for the preparation of the gelatine and its hydrolyzate which eliminates the problems connected with the preliminary defatting of the raw material in the form of the crumbled bones and especially the process which reduces the volume of the liquid wastes harmful for the environment and also lowers the level of the electric and thermal energy consumption.
The process of the invention for the preparation of the gelatine and its hydrolyzate consists in that the crumbled animal bones are subjected to the maceration process with the acid of the concentration not higher than 34% at the time from 1 to 14 days, and during the maceration or after its termination, the calcium salts are separated from the post-maceration lyes and the ossein obtained in this way, after the remaining acid is removed, preferably by rinsing with water, possibly containing the alkaline substance, is subjected to at least once extraction with the water at the temperature from 40 to 12000C. In order to obtain the gelatine, the water extract of the gelatine is cleaned by the use of the known methods, the extract is concentrated, possibly dried and milled, and in order to obtain the gelatine hydrolyzate, to the water extract there is added the proteolytic enzym which is later inactivated, and the extract is cleaned by the use of the known methods, concentrated and dried. The process of the invention is characterized in that the fat is removed from the reaction environment at the time of the maceration process and/or the extraction and/or after the termination of the maceration process and/or the extraction, by the separation of the water phase and the fatty phase or, in the case when the fat is removed after the termination of the extraction process, by the separation of the water phase containing the gelatine, the fatty phase and the solid phase or by the separation of the water phase containing the gelatine from the fatty phase combined with the solid phase.
The separation of the fatty phase and the water phase is carried out by the continuous or batch method.
Preferably the hydrochloric acid is used as the acid.
Before the stage of the maceration, the bones may be subjected to the proces of the muscle removal.
Preferably, the crumbled and possibly free of muscles animal bones are rinsed out with water. The process for the maceration is carried out with or without mixing of the reactor content.
Preferably, the acid for the maceration process is delivered to the reactor from its bottom and/or from its side, and the post-maceration lyes are collected from the top of the reactor.
Preferably, the acid for the maceration process is delivered from the top of the reactor, and the post- maceration lyes are collected from the bottom and/or from the side of the reactor.
Preferably, the acid for the maceration process is delivered from the side of the reactor, and the post- maceration lyes are collected from the top and/or from the bottom and/or from the side of the reactor.
Preferably, bones are classified by the kind of the animal species and/or the kind of the bones.
Preferably, the proteolytic enzym is added in the quantity of at least 0,01% in relation to the dry mass of the gelatine present in the extract.
Preferably, the proteolytic enzym is inactivated by rising the temperature of the extract containing the gelatine.
The substance of the invention is the removal of the fat at the stage and/or after the stage of the extraction and/or the maceration, but not, as in the known processes, before the bone raw material is subjected to maceration with the acid. The change of the defatting stage to the phase of the maceration and/or extraction enables the significant reduction of the volume of the liquid wastes formed in process. It happens thanks to the elimination of a large quantity of water introduced according to the process of the invention in which the whole first stage of the process for the preparation of the gelatine, namely the production of the defatted bone shot, is omitted. The bone material received from the meat processing plants and other sources should be only crumbled and then, without the preliminary defatting and without drying, is transfered to the production of the gelatine. Possibly, the bones are subjected to the process of the muscles removal if this process has not been earlier carried out in the meat processing plant. As a result, the whole module of the machines and devices for the preparation of the defatted bone shot and the installations and the production areas connected with them are eliminated. It leads to very big savings of the electric and thermal energy and a significant reduction of the costs connected with processing of the liquid wastes containing some quantities of the fat and proteins as well as a significant reduction of the costs for the preparation of the final product. The fat removed at the extraction stage contains water in a much lower quantity and thanks to that the fat separation may be much more easier and cheaper. The fat may be later used as the raw material in different applications, among others in the chemical industry.
The process of the invention is presented in more details in the realization example, and the schema of the process of the gelatine production is exemplary illustrated in the figure.
Example 1.
The pork bones from the meat processing plants and other sources along with the remaining meat tissue are crumbled onto pieces of the size from 1 to 10 mm and rinsed out with cold water in order to remove the remainder of the blood. The crumbled bones are introduced to the reactor and flooded repeatedly with hydrochloric acid of the concentration of 3,8% at the volume ratio of the bones to the acid solution of 1:2,27 until the macerated bones is obtained. In the meantime, the calcium salts are separated from the post-maceration lyes by precipitation. After the termination of the maceration, which takes from 1 to 14 days, the ossein produced is washed with water in order to remove the acid until pH not ecxeeding 5 is obtained. Next, the ossein is flooded with water in the quantity of no more than 5 volumes of the ossein and heated to the temperature of 500C. The extraction process is carried out several times until the gelatine is transfered from the ossein to the water solution, and next the gelatine solution in the water is collected from the reactor. The fatty phase is periodicaly removed by pumping out from the upper part of the reactor. The water phase with the gelatine is transfered from the reactor to the tanks, and next it is cleaned, deionized, possibly by the ultrafiltration. Then, there is carried out the concentration in the evaporators, cooling, drying, milling, mixing and packing of the final product. The residue after the extraction process is withdrawn from the reactor in order to separate the remaining fat, the gelatine solution and solid parts. The gelatine obtained has the gel hardness of 253 bloom.
Example 2
The pork bones from the meat processing plants and other sources along with the remaining meat tissue are crumbled onto pieces of the size from 1 to 10 mm. The crumbled bones are introduced to the reactor and flooded repeatedly with hydrochloric acid of the concentration of 4,2% at the volume ratio of the bones to the acid solution of 1:2,5 until the macerated bones are obtained. In the meantime, the calcium salts are separated from the post- maceration lyes by precipitation. After the termination of the maceration, which takes from 1 to 14 days, the ossein produced is washed with water in order to remove the acid until pH not ecxeeding 5 is obtained. Next, the ossein is flooded with water in the quantity of no more than 5 volumes of the ossein and heated to the temperature of 55°C. The extraction process is carried out several times until the gelatine is transfered from the ossein to the water solution, and next the gelatine solution in the water is collected from the reactor. After the termination of the extraction process the residue present in the reactor is transfered to a separate tank in which the preliminary collection of the fat is carried out by pumping out. Then, the residue is transfered to the decanter where the remainig fat, the water phase containing the gelatine and the solid phase are separated. The water phases containing the gelatine from the extraction stage and collected from the decanter are cleaned and deionized, possibly by ultrafiltration. The subsequent stages include concentration on the evaporators, cooling, drying, milling, mixing and packing of the final product. The gelatine obtained has the gel hardness of 302 bloom.
Example 3
From the pork bones coming from the meat processing plants and other sources the meat tissue is removed and then they are crumbled onto pieces of the size from 1 to 10 mm and rinsed out with cold water in order to remove the remainder of the blood. The crumbled bones are introduced to the reactor and flooded repeatedly with hydrochloric acid of the concentration of 3,5% at the volume ratio of the bones to the acid solution of 1:2,25 until the macerated bones are obtained. In the meantime, the calcium salts are separated from the post-maceration lyes by precipitation and periodically the fatty phase is separated from the upper part of the reactor. During the maceration stage about 20% of the fat is removed. After the termination of the maceration, which takes from 1 to 14 days, the ossein produced is washed with water with the addition of the base in order to remove the acid until pH not ecxeeding 5 is obtained. Next, the ossein is flooded with water in the quantity of no more than 5 volumes of the ossein and heated to the temperature of 99°C. The extraction process is carried out several times increasing the temperature until the gelatine from the ossein is transfered to the water solution, and next the gelatine solution in the water is collected from the reactor. During each extraction the fatty phase is periodicaly removed by pumping out from the upper part of the reactor. The water phase with the gelatine is transfered from the reactor to the tanks. The residue after the extraction process is withdrawn from the reactor in order to separate the remaining fat, the gelatine solution and solid parts. The water phases containing the gelatine are cleaned, deionized, possibly by ultrafiltration, and concentrated on the evaporators, cooled, dried, milled, mixed and packed as the final product. The gelatine obtained has the gel hardness of 248 bloom. Example 4
The pork bones from the meat processing plants and other sources along with the remaining meat tissue are crumbled onto pieces of the size from 1 to 10 mm. The crumbled bones are introduced to the reactor and flooded repeatedly with hydrochloric acid of the concentration of 4,2% at the volume ratio of the bones to the acid solution of 1:2,5 until the macerated bones are obtained. In the meantime, the calcium salts are separated from the post- maceration lyes by precipitation. After the termination of the maceration, which takes from 1 to 14 days, the ossein produced is washed with water in order to remove the acid until pH not ecxeeding 5,1 is obtained. Next, the ossein is flooded with water in the quantity of no more than 5 volumes of the ossein and heated to the temperature of 58°C. The extraction process is carried out several times until the gelatine is transfered from the ossein to the water solution, and next the gelatine solution in the water is collected from the reactor. After the termination of the extraction process, the residue present in the reactor is transfered to the separate tank in which the preliminary collection of the fat is carried out by pumping out. Then, the residue is transfered to the decanter where the remainig fat, the water phase containing the gelatine and the solid phase are separated. To the water phase containing the gelatine originated from the extraction ' stage and collected from the decanter there is added the base in order to increase pH to 7,5 and then the proteolytic enzym Bacillus amyloliquefacies (Mulitfect P-3000) is added in the quantity of 0,5% in relation to the dry mass of the gelatine present in the water phase. The base and enzym are added with the continuous mixing of the reactor content. After 1 hour, the temperature of the extract is increased to 800C in order to inactivate the enzym and then the extract is cleaned, concentrated and spray-dried.

Claims

Claims :
1. The process for the preparation of the gelatine and its hydrolyzate comprising the subjecting the crumbled animal bones to the maceration process with the acid of the concentration not higher than 34% at the time from 1 to 14 days, separating the calcium salts during the maceration or after its termination, removing the remaining acid, possibly by addition of the alkaline substance and then subjecting the ossein obtained in this way to at least once extraction with water of the temperature from 40 to 12000C, possibly in the case of production of the gelatine hydrolyzate, adding the proteolytic enzyme and its later inactivation, and next cleaning the water extract of the gelatine or the gelatine hydrolyzate, concentrating the extract, possibly drying and possibly milling, characterized in that the fat is removed from the reaction environment at the time of the maceration process and/or extraction and/or after the termination of the maceration process and/or extraction, by separation of the water phase containing the gelatine and the fatty phase or, in the case when the fat is removed after the termination of the extraction process, by separation of the water phase containing the gelatine, the fatty phase and the solid phase or by separation of the water phase containing the gelatine from the fatty phase combined with the solid phase.
2. The process of claim 1 characterized in that the removal of the fat is carried out in the continuous process.
3. The process of claim 1 characterized in that the removal of the fat is carried out in the batch process.
4. The process of claim 1 characterized in that hydrochloric acid is used as an acid.
5. The process of claim 1 characterized in that before the maceration process the bones are subjected to the proces of the muscle removal.
6. The process of claim 1 characterized in that the crumbled and possibly free of muscles animal bones are rinsed out with water.
7. The process of claim 1 characterized in that the maceration process is carried out with mixing of the reactor content.
8. The process of claim 1 characterized in that the maceration process is carried out without mixing of the reactor content.
9. The process of claim 1 characterized in that the acid for the maceration process is delivered to the reactor from its bottom and/or from its side, and the post- maceration lyes are collected from the top of the reactor.
10. The process of claim 1 characterized in that the acid for the maceration process is delivered from the top of the reactor, and the post-maceration lyes are collected from the bottom and/or from the side of the reactor.
11. The process of claim 1 characterized in that the acid for the maceration process is delivered from the side of the reactor, and the post-maceration lyes are collected from the top and/or from the bottom and/or from the side of the reactor.
12. The process of claim 1 characterized in that the bones are classiffied by the kind of the animal species and/or the kind of the bones.
13. The process of claim 1 characterized in that the proteolytic enzym is added in the quantity of at least 0,01% in relation to the dry mass of the gelatine present in the extract.
14. The process of claim 1 characterized in that the proteolytic enzym is inactivated by rising the temperature of the extract containing the gelatine.
PCT/PL2006/000028 2005-05-12 2006-05-10 Process for the preparation of gelatine and gelatine hydrolyzate WO2006121361A1 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2021089244A1 (en) * 2019-11-08 2021-05-14 Gelita Ag Method for the producing bone gelatine, and bone gelatine produced according to said method
WO2021089243A1 (en) * 2019-11-08 2021-05-14 Gelita Ag Method for producing collagen peptides from bones, and produced collagen peptides
CN115044300A (en) * 2022-06-23 2022-09-13 山东恒鑫生物科技有限公司 Method for producing gelatin for candy by using cow leather

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB247347A (en) * 1925-01-06 1926-02-18 Cecil Howard Shearman Improved method for the extraction of glue and fatty matters from bones and the like
US1951260A (en) * 1930-02-13 1934-03-13 Firm Ag Fur Chemische Produkte Method of producing glue from bones
US2215528A (en) * 1938-06-29 1940-09-24 William V Knoll Apparatus for extracting gelatin and glue
US2577429A (en) * 1945-11-23 1951-12-04 Camillo J Mueller Extraction apparatus
DE2136769A1 (en) * 1971-07-22 1973-02-08 Pfeffer Chem Werke Tannery wastes processing - to produce gelatine, fat and fodder additive
DD200156A1 (en) * 1981-08-06 1983-03-23 Wolfgang Baum METHOD FOR SEPARATING A MEAT, FAT AND BONE MIXTURE
DE3610025A1 (en) * 1985-03-26 1986-10-02 Herbert 74379 Ingersheim Rieger Process and tank for producing gelatine
WO1994021739A1 (en) * 1993-03-19 1994-09-29 Ellco Food Ab Method for producing gelatin
CN1151222C (en) * 2001-04-08 2004-05-26 内蒙古草原兴发股份有限公司 Process for preparing bone collagen

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB247347A (en) * 1925-01-06 1926-02-18 Cecil Howard Shearman Improved method for the extraction of glue and fatty matters from bones and the like
US1951260A (en) * 1930-02-13 1934-03-13 Firm Ag Fur Chemische Produkte Method of producing glue from bones
US2215528A (en) * 1938-06-29 1940-09-24 William V Knoll Apparatus for extracting gelatin and glue
US2577429A (en) * 1945-11-23 1951-12-04 Camillo J Mueller Extraction apparatus
DE2136769A1 (en) * 1971-07-22 1973-02-08 Pfeffer Chem Werke Tannery wastes processing - to produce gelatine, fat and fodder additive
DD200156A1 (en) * 1981-08-06 1983-03-23 Wolfgang Baum METHOD FOR SEPARATING A MEAT, FAT AND BONE MIXTURE
DE3610025A1 (en) * 1985-03-26 1986-10-02 Herbert 74379 Ingersheim Rieger Process and tank for producing gelatine
WO1994021739A1 (en) * 1993-03-19 1994-09-29 Ellco Food Ab Method for producing gelatin
CN1151222C (en) * 2001-04-08 2004-05-26 内蒙古草原兴发股份有限公司 Process for preparing bone collagen

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
DATABASE WPI Section Ch Week 200617, Derwent World Patents Index; Class G03, AN 2002-305637, XP002398073 *

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2021089244A1 (en) * 2019-11-08 2021-05-14 Gelita Ag Method for the producing bone gelatine, and bone gelatine produced according to said method
WO2021089243A1 (en) * 2019-11-08 2021-05-14 Gelita Ag Method for producing collagen peptides from bones, and produced collagen peptides
CN114845560A (en) * 2019-11-08 2022-08-02 嘉利达股份有限公司 Method for producing collagen peptide from bone and collagen peptide produced thereby
CN115044300A (en) * 2022-06-23 2022-09-13 山东恒鑫生物科技有限公司 Method for producing gelatin for candy by using cow leather
CN115044300B (en) * 2022-06-23 2023-05-02 山东恒鑫生物科技有限公司 Method for producing gelatin for candies by using cowhide

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