METHOD FOR UTILIZING INTERNALLY GENERATED BIOGAS FOR CLOSED MEMBRANE SYSTEM OPERATION
    1.
    发明申请
    METHOD FOR UTILIZING INTERNALLY GENERATED BIOGAS FOR CLOSED MEMBRANE SYSTEM OPERATION 审中-公开
    利用内部产生的生物气体进行闭式膜系统操作的方法

    公开(公告)号:WO2012030449A3

    公开(公告)日:2012-04-19

    申请号:PCT/US2011045651

    申请日:2011-07-28

    Abstract: In an anaerobic membrane bioreactor ("MBR"), a closed anaerobic process tank contains a membrane filter or is connected to an external tank containing a membrane filter. A pocket of biogas accumulates at the top of the process tank. Biogas is taken from the pocket, pumped to the bottom of the membrane filter to provide bubbles to inhibit membrane fouling, and returned to the pocket. Excess biogas produced as the wastewater is degraded is removed from the system and may be used as a product. However, biogas and liquid are maintained in the system at a pressure above atmospheric, for example 10 kPa or more above atmospheric pressure, sufficient to provide at least a material contribution to the transmembrane pressure driving permeation through the membranes. The overall energy requirements of the system may be reduced. Further, with sufficient pressure, suction pumps attached to the membranes may not be required.

    Abstract translation: 在厌氧膜生物反应器(“MBR”)中,封闭的厌氧处理罐包含膜过滤器或连接至含有膜过滤器的外部罐。 处理罐顶部积聚了一袋沼气。 将沼气从口袋中取出,泵入膜过滤器的底部以提供气泡以抑制膜结垢,并将其返回口袋。 随着废水降解产生的过量沼气将从系统中排出并可用作产品。 然而,沼气和液体在高于大气压的压力下保持在系统中,例如高于大气压的10kPa或更高,足以提供至少对通过膜的跨膜压力驱动渗透的材料贡献。 系统的整体能量需求可能会降低。 此外,在足够的压力下,可能不需要连接到膜上的抽吸泵。

    METHOD FOR UTILIZING INTERNALLY GENERATED BIOGAS FOR CLOSED MEMBRANE SYSTEM OPERATION
    2.
    发明申请
    METHOD FOR UTILIZING INTERNALLY GENERATED BIOGAS FOR CLOSED MEMBRANE SYSTEM OPERATION 审中-公开
    用于封闭膜系统操作的内部生物生物学方法

    公开(公告)号:WO2012030449A2

    公开(公告)日:2012-03-08

    申请号:PCT/US2011/045651

    申请日:2011-07-28

    Abstract: In an anaerobic membrane bioreactor ("MBR"), a closed anaerobic process tank contains a membrane filter or is connected to an external tank containing a membrane filter. A pocket of biogas accumulates at the top of the process tank. Biogas is taken from the pocket, pumped to the bottom of the membrane filter to provide bubbles to inhibit membrane fouling, and returned to the pocket. Excess biogas produced as the wastewater is degraded is removed from the system and may be used as a product. However, biogas and liquid are maintained in the system at a pressure above atmospheric, for example 10 kPa or more above atmospheric pressure, sufficient to provide at least a material contribution to the transmembrane pressure driving permeation through the membranes. The overall energy requirements of the system may be reduced. Further, with sufficient pressure, suction pumps attached to the membranes may not be required.

    Abstract translation: 在厌氧膜生物反应器(“MBR”)中,封闭的厌氧处理罐包含膜过滤器或连接到含有膜过滤器的外部罐。 沼气袋在加工罐顶部积聚。 将沼气从口袋中取出,泵送到膜过滤器的底部以提供气泡以阻止膜污染,并返回到口袋中。 随着废水的降解而产生的过量生物气体被从系统中除去,可以用作产品。 然而,生物气体和液体在高于大气压的压力下保持在系统中,例如高于大气压力10kPa或更高,足以提供至少一种材料对穿过膜的透过膜的压力驱动。 系统的总体能量需求可能会降低。 此外,在足够的压力下,可能不需要连接到膜的抽吸泵。

    TORQUE-BALANCED, GAS-SEALED WIRELINE CABLES
    4.
    发明申请
    TORQUE-BALANCED, GAS-SEALED WIRELINE CABLES 审中-公开
    TORQUE-BALANCED,气密封线缆

    公开(公告)号:WO2010121015A2

    公开(公告)日:2010-10-21

    申请号:PCT/US2010/031218

    申请日:2010-04-15

    Abstract: A torque-balanced, gas-blocking wireline cable and a method of making the cable includes an electrically conductive cable core for transmitting electrical power and surrounding inner and outer layers of a plurality of armor wires. Gas blocking is achieved by placing a soft polymer layer over the core before the inner wires are cabled thereon. The inner wires imbed partially into the soft polymer layer such that no gaps are left between the inner wires and the core. A second soft polymer layer is optionally extruded over the inner wires before the outer wires are applied. The second soft polymer layer fills any spaces between the inner and outer wire layers and prevents pressurized gas from infiltrating between the wires. The inner wires have larger diameters than the outer wires such that the inner wires carry approximately 60 % of the load and torque imbalance is prevented.

    Abstract translation: 扭矩平衡的阻气电缆电缆和制造电缆的方法包括用于传输电力并围绕多个铠装线的内层和外层的导电电缆芯。 气体阻塞是通过将软聚合物层置于芯上而实现的,然后将内部导线连接在芯上。 内部线材部分地嵌入软质聚合物层中,使得内部线材和芯部之间没有间隙。 在施加外部电线之前,第二软聚合物层任选地在内部电线上挤出。 第二软聚合物层填充内部和外部线层之间的任何空间,并且防止加压气体渗入电线之间。 内部线材的直径大于外部线材,因此内部线材承载大约60%的负载,并且防止扭矩不平衡。

    SOY PROCESSING METHOD USING SPECIFIC ENZYME, PROCESSED SOY POWDERAND PROCESSED SOY LIQUID
    5.
    发明申请
    SOY PROCESSING METHOD USING SPECIFIC ENZYME, PROCESSED SOY POWDERAND PROCESSED SOY LIQUID 审中-公开
    使用特殊酶的大量加工方法,加工大豆粉加工大豆液

    公开(公告)号:WO2007028222A2

    公开(公告)日:2007-03-15

    申请号:PCT/BR2006000179

    申请日:2006-09-06

    Inventor: KAI CHANG SHENG

    CPC classification number: C12Y302/01015 A23L11/09

    Abstract: The present invention refers to a method of processing soy by using specific enzyme, in other words, by using a pectinase produced by microorganisms from Aspergillus genre (such as pectinmetilesterase enzyme, produced by the microorganism Aspergillus oryzae; or the enzymes pectintranseliminase, poligalacturonase and pectinesterase, produced by the microorganism Aspergillus niger; or betagluconase (endo- 1,3(4)-), produced by the microorganism Aspergillus aculeatus), which is capable of efficiently producing a processed soy powder and/or liquid with substantially no unpleasant odor, characteristic of products derived from soy, and an ameliorated digestion-absorption coefficient for human body for the human body, using soy in its integral form, in other words, utilizing all nutrients present in soy. It also refers to a processed soy powder and/or liquid with substantially no unpleasant odor, characteristic of products derived from soy, and an ameliorated digestion-absorption coefficient for human body, using soy in its whole form.

    Abstract translation: 本发明涉及通过使用特定酶处理大豆的方法,换句话说,通过使用由曲霉类型的微生物产生的果胶酶(例如由微生物米曲霉产生的果胶多肽酶)或者果胶转移酶,聚葡萄糖聚糖酶和果胶泛酸酶 由微生物黑曲霉生产的;或由微生物曲霉(Aspergillus aculeatus)生产的betagluconase(end-1,3(4) - )),其能够有效地生产基本上没有令人不快的气味的加工大豆粉和/或液体, 来自大豆的产品的特征,以及人体对人体的消化吸收系数的改善,使用其整体形式的大豆,换句话说,利用大豆中存在的所有营养物质。 它还涉及使用大豆整体形式的基本没有令人不愉快的气味的加工大豆粉和/或液体,来自大豆的产品的特征以及改善的人体的消化吸收系数。

    LIQUID OPTICAL DEFLECTOR AND METHOD FOR FABRICATING THE SAME
    7.
    发明申请
    LIQUID OPTICAL DEFLECTOR AND METHOD FOR FABRICATING THE SAME 审中-公开
    液态光学偏转器及其制造方法

    公开(公告)号:WO2009100584A8

    公开(公告)日:2009-11-05

    申请号:PCT/CN2008000327

    申请日:2008-02-05

    CPC classification number: G02B26/004

    Abstract: A liquid optical deflector comprises a substrate (100) with an electrode layer (102) disposed on the substrate (100). An insulating layer (104) is on the electrode layer (102), which having an exposed region. A first electrode wall (106A) provided with a first insulating wall (108) and a second electrode wall (106B) provided with a second insulating wall (108) right up from the substrate (100). A side wall rights up from the substrate and connects between the first and second electrode walls (106A, 106B) to form a containing space. A first liquid (110) is filled in the containing space in contacting with the electrode layer (102) on the substrate (100). A second liquid (112) is filled in the containing space to have an interface with the first liquid (110) without solving to each other. A cap layer (114) seals over the containing space to form an optical deflector unit.

    Abstract translation: 液体光学偏转器包括具有设置在基板(100)上的电极层(102)的基板(100)。 绝缘层(104)位于具有暴露区域的电极层(102)上。 第一电极壁(106A)设置有第一绝缘壁(108)和第二电极壁(106B),第二电极壁(106B)设置有从衬底(100)向上的第二绝缘壁(108)。 侧壁从基板向上设置并且连接在第一和第二电极壁(106A,106B)之间以形成容纳空间。 第一液体(110)填充在容纳空间中,与基板(100)上的电极层(102)接触。 第二液体(112)填充在容纳空间中以与第一液体(110)具有界面而不会相互解决。 盖层(114)密封在容纳空间上以形成光学偏转器单元。

    WASTEWATER TREATMENT WITH AEROBIC GRANULES
    9.
    发明申请
    WASTEWATER TREATMENT WITH AEROBIC GRANULES 审中-公开
    废水处理与无机颗粒

    公开(公告)号:WO2008141413A1

    公开(公告)日:2008-11-27

    申请号:PCT/CA2007/000893

    申请日:2007-05-18

    Abstract: A wastewater treatment system using aerobic granules has a large number of sequencing batch reactor tanks with high volumetric exchange rate, a variable cycle length and constant batch volume. The batch reactors are operated for C, N removal and P is removed chemically. SS are removed in a downstream separation step. A continuous flow reactor may comprise an aerobic zone, an alternately aerobic and anoxic zone or discrete aerobic and anoxic zones, and a settling zone. An anaerobic zone may be located at the bottom of a mass of settled granules. Feed may be introduced through the settled granules. An aerobic/anoxic zone may be like a CSTR but with aeration varying in space or time. Sludge granules may move intermittently from an aerobic zone to an aerobic/anoxic zone. A settling zone may have an upflow rate to wash off flocculated biomass. A dual sludge process may be used in which a fraction of unsettled floc is recycled to a region upstream of the granules settler. A fermentation zone may be used to pre-treat feed water or to treat a recycled waste stream, for example a waste stream contain floc.

    Abstract translation: 使用有氧颗粒的废水处理系统具有大量的具有高体积交换速率,可变循环长度和恒定批量体积的间歇式反应釜。 操作间歇式反应器用于C,N去除,P被化学去除。 SS在下游分离步骤中被去除。 连续流动反应器可包括需氧区,交替需氧和缺氧区或离散的有氧和缺氧区以及沉降区。 厌氧区可以位于大量沉降颗粒的底部。 饲料可以通过沉降的颗粒引入。 有氧/缺氧区域可能类似于CSTR,但是曝气在空间或时间上变化。 污泥颗粒可以间歇地从需氧区移动到需氧/缺氧区。 沉降区可以具有上升流速以洗脱絮凝生物质。 可以使用双重污泥方法,其中一部分不稳定的絮体再循环到颗粒沉降器上游的区域。 发酵区可用于预处理给水或处理回收的废物流,例如含有絮凝物的废物流。

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