MEDINA Sara (CA),МЕДИНА Сара (CA),SIGALL Kevin I. (CA),СИГАЛЛ Кевин И. (CA),GRIN Brent I. (CA),ГРИН Брент И. (CA),ShVAJTsER Martin (CA),ШВАЙЦЕР Мартин (CA),MEDINA SARA,МЕДИНА Сара,SIGALL KEVIN I.,СИГАЛЛ Кевин И.,GRIN BRENT I.,ГРИН Брент И.,SHVAJTSER MARTIN,ШВАЙЦЕР Мартин
申请号：
RU2011150821/10
公开号：
RU0002531237C2
申请日:
2010.04.23
申请国别(地区):
RU
年份:
2014
代理人:
摘要：
FIELD: food industry.SUBSTANCE: invention relates to food industry. The canola protein product is manufactured by way of partial concentration of a supernatant produced during canola protein micellar mass sedimentation till concentration is equal to 50 g/l or less or by way of concentration of a supernatant produced during canola protein micellar mass sedimentation till concentration is equal to at least 50 g/l. One adds a calcium salt to the supernatant produced without concentration stage, to provide for conductivity equal to 5 - 30 mSm, or to the partially concentrated supernatant to provide for conductivity equal to 2 - 30 mSm till calcium phytate sediment formation. The sedimented calcium phytate is removed from the produced solution till production of a clear solution. Optionally, the clear solution pH is regulated till the value is equal to 2.0 - 4.0. In case of concentration stage absence or partial concentration stage presence one performs the clear solution concentration till concentration is equal to at least 50 g/l. According to another version, one performs addition of initial quantity of a calcium salt to the supernatant produced during canola protein micellar mass sedimentation till conductivity is equal to 1 - 3.5 mSm which is insufficient for calcium phytate sedimentation stimulation. pH is regulated till the value is equal to 2.0 - 4.0； one performs partial concentration till concentration is equal to 50 g/l or less. One adds additional quantity of the calcium salt to provide for conductivity equal to 4 - 30 mSm till sediment formation. The sediment is removed from the produced solution； the clear solution is concentrated till concentration is equal to at least 50 g/l, optionally, diafiltered and decoloured. The produced protein solution is dried. The concentration and/or diafiltration stage is/are performed so that the dry canola protein product approximately contains from 60 to less than 90 wt % (N×6.25) of protein in terms of dry substance weigh
