Continuous process for production of oil seed protein isolate
    1.
    发明授权
    Continuous process for production of oil seed protein isolate 有权
    生产油籽蛋白分离物的连续工艺

    公开(公告)号:US07625588B2

    公开(公告)日:2009-12-01

    申请号:US12230303

    申请日:2008-08-27

    CPC分类号: C07K14/415 A23J1/14

    摘要: Oil seed protein isolates, particularly canola protein isolate, are produced continuously from oil seed meals, preferably at a high purity level of at least about 100 wt % (N×6.25), by a process wherein oil seed protein is continuously extracted from oil seed meal, the resulting protein solution is continuously concentrated, preferably to a protein content of at least about 200 g/L, and the concentrated protein solution is continuously mixed with chilled water having a temperature below about 15° C. to form protein micellar, which are settled in the settling vessel to provide a protein micellar mass (PMM) while supernatant overflows the vessel. The PMM, when accumulated to a desired degree, may be separated from supernatant and dried. The supernatant may be processed to recover additional oil seed protein isolate.

    摘要翻译: 油籽蛋白分离物,特别是卡诺拉蛋白分离物,通过其中从油籽连续提取油籽蛋白的方法,从油籽菜中连续生产,优选至少约100重量%(N×6.25)的高纯度水平, 将所得到的蛋白质溶液连续浓缩,优选至少为约200g / L的蛋白质含量,并将浓缩的蛋白质溶液与温度低于约15℃的冷冻水连续混合以形成蛋白质胶束,其中 沉降在沉淀容器中以提供蛋白质胶束质量(PMM),而上清液溢出血管。 当PMM累积到所需程度时,可以与上清液分离并干燥。 可以处理上清液以回收另外的油籽蛋白分离物。

    Continuous process for production of oil seed protein isolate
    2.
    发明申请
    Continuous process for production of oil seed protein isolate 有权
    生产油籽蛋白分离物的连续工艺

    公开(公告)号:US20080319171A1

    公开(公告)日:2008-12-25

    申请号:US12230199

    申请日:2008-08-26

    IPC分类号: C07K14/415

    CPC分类号: C07K14/415 A23J1/14

    摘要: Oil seed protein isolates, particularly canola protein isolate, are produced continuously from oil seed meals, preferably at a high purity level of at least about 100 wt % (Nx 6.25), by a process wherein oil seed protein is continuously extracted from oil seed meal, the resulting protein solution is continuously concentrated, preferably to a protein content of at least about 200 g/L, and the concentrated protein solution is continuously mixed with chilled water having a temperature below about 15° C. to form protein micellar, which are settled in the settling vessel to provide a protein micellar mass (PMM) while supernatant overflows the vessel. The PMM, when accumulated to a desired degree, may be separated from supernatant and dried. The supernatant may be processed to recover additional oil seed protein isolate.

    摘要翻译: 油籽蛋白分离物,特别是卡诺拉蛋白分离物,通过油籽种子餐连续提取,油籽蛋白从油籽粉中连续提取的方法,优选以至少约100重量%(N×6.25)的高纯度水平连续生产, ,所得蛋白质溶液被连续浓缩,优选至少为约200g / L的蛋白质含量,并将浓缩的蛋白质溶液与温度低于约15℃的冷冻水连续混合以形成蛋白质胶束,其为 沉降在沉淀容器中以提供蛋白质胶束质量(PMM),同时上清液溢出血管。 当PMM累积到所需程度时,可以与上清液分离并干燥。 可以处理上清液以回收另外的油籽蛋白分离物。

    Continuous process for production of oil seed protein isolate
    3.
    发明授权
    Continuous process for production of oil seed protein isolate 有权
    生产油籽蛋白分离物的连续工艺

    公开(公告)号:US07704534B2

    公开(公告)日:2010-04-27

    申请号:US12230199

    申请日:2008-08-26

    CPC分类号: C07K14/415 A23J1/14

    摘要: Oil seed protein isolates, particularly canola protein isolate, are produced continuously from oil seed meals, preferably at a high purity level of at least about 100 wt % (Nx 6.25), by a process wherein oil seed protein is continuously extracted from oil seed meal, the resulting protein solution is continuously concentrated, preferably to a protein content of at least about 200 g/L, and the concentrated protein solution is continuously mixed with chilled water having a temperature below about 15° C. to form protein micellar, which are settled in the settling vessel to provide a protein micellar mass (PMM) while supernatant overflows the vessel. The PMM, when accumulated to a desired degree, may be separated from supernatant and dried. The supernatant may be processed to recover additional oil seed protein isolate.

    摘要翻译: 油籽蛋白分离物,特别是卡诺拉蛋白分离物,通过油籽种子餐连续提取,油籽蛋白从油籽粉中连续提取的方法,优选以至少约100重量%(N×6.25)的高纯度水平连续生产, ,所得蛋白质溶液被连续浓缩,优选至少为约200g / L的蛋白质含量,并将浓缩的蛋白质溶液与温度低于约15℃的冷冻水连续混合以形成蛋白质胶束,其为 沉降在沉淀容器中以提供蛋白质胶束质量(PMM),同时上清液溢出血管。 当PMM累积到所需程度时,可以与上清液分离并干燥。 可以处理上清液以回收另外的油籽蛋白分离物。

    Continuous process for production of oil seed protein isolate

    公开(公告)号:US20090076252A1

    公开(公告)日:2009-03-19

    申请号:US12230303

    申请日:2008-08-27

    IPC分类号: C07K1/14

    CPC分类号: C07K14/415 A23J1/14

    摘要: Oil seed protein isolates, particularly canola protein isolate, are produced continuously from oil seed meals, preferably at a high purity level of at least about 100 wt % (N×6.25), by a process wherein oil seed protein is continuously extracted from oil seed meal, the resulting protein solution is continuously concentrated, preferably to a protein content of at least about 200 g/L, and the concentrated protein solution is continuously mixed with chilled water having a temperature below about 15° C. to form protein micellar, which are settled in the settling vessel to provide a protein micellar mass (PMM) while supernatant overflows the vessel. The PMM, when accumulated to a desired degree, may be separated from supernatant and dried. The supernatant may be processed to recover additional oil seed protein isolate.

    Production of flax protein isolate
    5.
    发明授权
    Production of flax protein isolate 有权
    生产亚麻蛋白分离物

    公开(公告)号:US07820226B2

    公开(公告)日:2010-10-26

    申请号:US10493110

    申请日:2002-10-10

    IPC分类号: C07K14/415

    CPC分类号: A23J1/142 A23J1/14 A23J3/14

    摘要: Flax and linola oil seed protein isolated are provided. Such isolates are made by extracting flax and linola oil seed protein from the oil seed meal, concentrating the aqueous protein solution, diluting the concentrated protein solution to form protein micelles, collecting mass. Further flax protein isolate may be recovered from the supernatant from the protein micellar formation. The protein isolated have a protein content of at least about 90 wt % (N ×6.25), preferably at least about 100 wt %, on a dry weight basis.

    摘要翻译: 提供了亚麻和线索油籽蛋白分离。 这种分离物是通过从油籽粉中提取亚麻籽油和亚麻籽油种子蛋白质,浓缩蛋白质水溶液,稀释浓缩的蛋白质溶液形成蛋白胶束,收集质量。 可以从蛋白质胶束形成的上清液中回收另外的亚麻蛋白分离物。 分离的蛋白质的蛋白质含量基于干重至少约90重量%(N×6.25),优选至少约100重量%。