METHOD OF INCREASING WATER SOLUBLE NUTRIENT EXTRACTION FROM PLANT MATTER

    公开(公告)号:WO2018182762A1

    公开(公告)日:2018-10-04

    申请号:PCT/US2017/033537

    申请日:2017-05-19

    Inventor: WICHMANN, Todd

    Abstract: Improved processes for extracting water soluble nutrients including sugars from plants and in particular sugar cane. The plants may be washed with a wash solution. After washing, water soluble nutrient containing liquid is extracted from the plants. A diluted wash solution may be added to the crushed plants to improve the extraction of the water soluble nutrients. The wash solution may be added to the liquid collected during the extraction to improve the separation of impurities from the nutrient containing liquid. The extracted liquid may demonstrate at least one of improved purity, improved clarity, improved filtration times, improved whiteness, and improved total recovered water soluble nutrients.

    PROCESSING OF SWEET SORGHUM FOR BIOETHANOL PRODUCTION
    4.
    发明申请
    PROCESSING OF SWEET SORGHUM FOR BIOETHANOL PRODUCTION 审中-公开
    用于生产乙二醇的甜菜皂的加工

    公开(公告)号:WO2008029163A2

    公开(公告)日:2008-03-13

    申请号:PCT/GB2007003395

    申请日:2007-09-10

    Inventor: BADALOV ARSEN

    CPC classification number: C12P7/10 C13B10/02 C13K1/02 Y02E50/16

    Abstract: A method of processing sweet sorghum cane for sugar extraction is disclosed. The method comprises passing the cane into a first cutter (4) to cut the material coarsely and then passing the material into a second cutter (7) to cut it into fine fibres. The fibrous material is then passed to a press (10) to extract sugar juice for fermentation in a bioethanol production plant (25).

    Abstract translation: 公开了一种加工甜高粱用于糖提取的方法。 所述方法包括将所述拐杖通过第一切割器(4)以粗略地切割所述材料,然后将所述材料通入第二切割器(7)以将其切成细纤维。 然后将纤维材料送入压榨机(10)以提取用于在生物乙醇生产设备(25)中发酵的糖汁。

    IMPROVEMENTS IN OR IN RELATION TO SUGARCANE PROCESSING

    公开(公告)号:WO2022051805A1

    公开(公告)日:2022-03-17

    申请号:PCT/AU2021/051040

    申请日:2021-09-08

    Abstract: A slotted conveyor floor 16 in milling tandem, slots 34 extend across the direction of liquid flow shown by arrow 35 which is against the flow of fibre. The slots are cut through the material of floor 16 on the vertical as depicted by centre-line 35 taken relative to the inclination of floor 16. Thus the centre-line corresponds to gravity feed for the liquid. Rather than being directly across the floor 16, the slots are inclined in the direction of flow. The fibre is in the opposite flow relation to the liquid, in this example, the slots are across the line of the fibre and are about 6mm wide and 180mm long with about 60mm spacing. Adjacent lines of slots are set interdigital in the direction of travel. This arrangement minimises fibre being trapped in the slots as the fibre is being carried by the rakes up the floor.

    原料糖及び精製糖の製造プロセス

    公开(公告)号:WO2022014725A2

    公开(公告)日:2022-01-20

    申请号:PCT/JP2021/041858

    申请日:2021-11-15

    Inventor: 松山 貴久

    Abstract: 精製糖の製造プロセスの各工程における影響は勿論のこと、原料糖の製造プロセスの各工程にも大きな影響を与える微細な濁質分を微細泡から成るオゾンを用いて効率よく除去できるようにした原料糖及び精製糖の製造プロセスを創出することを課題とする。 甘味資源作物から精製糖を精製する製造プロセスであって、甘味資源作物から原料糖を製造する原料糖の製造プロセスと、原料糖から精製糖を精製する精製糖の製造プロセスを有し、原料糖の製造プロセスと精製糖の製造プロセスの少なくとも一方の製造プロセスに、微細泡から成るオゾンを糖液中に溶け込ませることにより、糖液中に含まれる微細な濁質分を分解除去するオゾン処理工程を備える構成とする。

    METHOD OF DISINTEGRATING AND FLUID DRYING OF SUGAR BEET MATERIAL PREVENTING THE DEGRADATION REACTION OF THE MATERIAL

    公开(公告)号:WO2021177902A1

    公开(公告)日:2021-09-10

    申请号:PCT/SK2020/050015

    申请日:2020-09-02

    Applicant: ŽITNÝ, Boris

    Inventor: ŽITNÝ, Boris

    Abstract: The invention relates to a method for the disintegration and fluid drying of sugar beet material which prevents the material's degradation reaction from taking place and which comprises the steps of disintegrating the sugar beet material to particles with a particle surface area of at least 2.0 cm2, and subsequent immediate exposure of the disintegrated material to a drying gas(es) at a temperature of 25°C to 160°C and a flow rate of 5 m.s-1 to 40 m.s-1, where the relative humidity of the drying gas(es) at the inlet to the drying space is at most 85%; and subsequent mixing of the disintegrated material with a flow of drying gas(es) until attaining a value of dry matter of at least 70% by weight.

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