METHOD FOR MANUFACTURING A HEAT EXCHANGER
    1.
    发明申请
    METHOD FOR MANUFACTURING A HEAT EXCHANGER 审中-公开
    制造热交换器的方法

    公开(公告)号:US20090194268A1

    公开(公告)日:2009-08-06

    申请号:US12438690

    申请日:2007-08-28

    IPC分类号: F28F7/00 B21D53/04

    摘要: The method for manufacturing a heat exchanger from a plastic material comprises feeding of at least two sheet elements, and, by means of shaping means, shaping of said sheet elements to form heat exchanger plates. The shaping means are adapted to also undertake joining the sheet elements partly along edges so that a fluid inlet and outlet are created, whereby the sheet elements are pressed together. The heat exchanger plates are stacked and joined to a heat exchanger. The stack of heat exchanger plates is welded so that the fluid inlets are fluid outlets of the respective heat exchanger plates are combined to form a common fluid inlet and a common fluid outlet, and the sides of the heat exchanger plates are welded together, so that a fully functional heat exchanger is manufactured with plastic sheets as the only raw material.

    摘要翻译: 用于从塑料材料制造热交换器的方法包括进料至少两个片状元件,并且通过成形装置进行所述片状元件的成形以形成热交换器板。 成型装置还适于部分地沿着边缘接合片状元件,从而产生流体入口和出口,由此片材被压在一起。 热交换器板被堆叠并接合到热交换器。 焊接堆叠的热交换器板,使得流体入口是相应热交换器板的流体出口组合以形成公共流体入口和公共流体出口,并且热交换器板的侧面被焊接在一起,使得 以塑料片作为唯一原料制造全功能热交换器。

    Drive arrangement for high-pressure pump and high-pressure cleaner with
such a drive arrangement
    2.
    发明授权
    Drive arrangement for high-pressure pump and high-pressure cleaner with such a drive arrangement 失效
    具有这种驱动装置的高压泵和高压清洁器的驱动装置

    公开(公告)号:US5793134A

    公开(公告)日:1998-08-11

    申请号:US780438

    申请日:1997-01-08

    IPC分类号: H02K7/06

    CPC分类号: H02K7/06

    摘要: In a drive arrangement for driving a pump of the axial-piston type, of which solely the swash-plate member (8) is shown, from a motor (1), the main novel feature is that the motor shaft (9) is directly connected or connectable to the swash-plate member (8), thus eliminating problems caused by a previously used intermediate shaft between the motor shaft and the swash-plate member.

    摘要翻译: 在用于驱动单轴旋转斜盘构件(8)所示的轴向 - 活塞式泵的驱动装置中,电动机(1)的主要特征是马达轴(9)直接 连接或连接到旋转斜盘部件(8),从而消除了电动机轴和旋转斜盘部件之间的先前使用的中间轴引起的问题。

    POLYMER ORGANOCATALYST AND PREPARATION PROCESS
    3.
    发明申请
    POLYMER ORGANOCATALYST AND PREPARATION PROCESS 审中-公开
    聚合物有机物和制备方法

    公开(公告)号:US20110034654A1

    公开(公告)日:2011-02-10

    申请号:US12812315

    申请日:2009-01-07

    IPC分类号: C08F126/06 C07C205/45

    CPC分类号: C08F26/06

    摘要: A chiral polymer organocatalyst comprising a main chain and side chain organocatalytic groups covalently attached to the main chain, which organocatalytic groups comprise an amino acid or amino acid derivative of the following general formula (I), in which one stereoisomeric form predominates: formula (I) wherein the catalyst is bound to the polymer main chain via R1, R2, R4, R5 or R6 through a linker (L) or direct bond, and wherein R1-R6 and Z are defined as follows: R1 is H, a naturally occurring alpha-amino acid side chain or a non-natural commercially available alpha-amino acid side chain that may contain L; R2 is H, O (doubly bonded to give a carbonyl), O-L (where L is a linker), NH-L or L; R3 is H or doubly bonded to give a carbonyl with R2 when R2 is O; R4 is H, C1-C6 alkyl or L R5 is H, CO2H, C1-C6 alkyl, benzyl, L, CONHR (in which R is alkyl, aryl, heteroaryl, arylalkyl or, heteroarylalkyl), tetrazolyl, CH2 coupled to a triazole moiety, an esterified CH2OH or CO2R (in which R is alkyl, aryl, heteroaryl, arylalkyl N or heteroarylalkyl), formula (II) or formula (III) wherein z is formula (IV) or a directed bond, X4 is H, Me3Si or Et3Si, X3 comprises a naturally-occurring alpha-amino acid side chain, H, C1-C6 alkyl or phenyl, Ar1 and Ar2 are each independently aryl or heteroaryl, and Y denotes the position of attachment to the main chain or linker; and R6 is H, CO2H3 C1-C6 alkyl, benzyl or L; and wherein the polymer organocatalyst comprises a cross-linked polymer.

    摘要翻译: 一种手性聚合物有机催化剂,其包含与主链共价连接的主链和侧链有机催化基团,该有机催化基团包含以下通式(I)的氨基酸或氨基酸衍生物,其中一种立体异构形式占主导地位:式(I )其中催化剂通过连接基(L)或直接键通过R 1,R 2,R 4,R 5或R 6与聚合物主链结合,并且其中R 1 -R 6和Z定义如下:R 1是H,天然存在的 α-氨基酸侧链或可以含有L的非天然的市售α-氨基酸侧链; R 2是H,O(双键合得到羰基),O-L(其中L是连接基),NH-L或L; 当R 2为O时,R 3为H或双键结合,得到具有R 2的羰基; R4是H,C1-C6烷基或L R5是H,CO2H,C1-C6烷基,苄基,L,CONHR(其中R是烷基,芳基,杂芳基,芳基烷基或杂芳基烷基),四唑基, 部分,酯化的CH 2 OH或CO 2 R(其中R是烷基,芳基,杂芳基,芳基烷基N或杂芳基烷基),式(II)或式(III)其中z是式(IV)或定向键,X 4是H,Me 3 Si 或Et 3 Si,X 3包含天然存在的α-氨基酸侧链,H,C 1 -C 6烷基或苯基,Ar 1和Ar 2各自独立地为芳基或杂芳基,Y表示与主链或连接基连接的位置。 并且R 6是H,CO 2 H 3 C 1 -C 6烷基,苄基或L; 并且其中所述聚合物有机催化剂包含交联聚合物。

    Method for production of a vegetable protein hydrolyzate with proteases
    4.
    发明授权
    Method for production of a vegetable protein hydrolyzate with proteases 失效
    用蛋白酶生产植物蛋白水解产物的方法

    公开(公告)号:US5716801A

    公开(公告)日:1998-02-10

    申请号:US417715

    申请日:1995-04-06

    CPC分类号: A23J3/346

    摘要: A well tasting and organoleptically acceptable vegetable protein hydrolyzate such as soy, pea or rice protein hydrolyzate is produced in high yield by a method using a combination of non-pH-stat hydrolysis and ultrafiltration. Preferably, the method is carried out by mixing a material containing at least 65% vegetable protein as dry matter and water to form a slurry containing a vegetable protein content of about 7-20%, heating the slurry to above 60.degree. C., adjusting the pH of the slurry to about 8.5, hydrolyzing the slurry with at least two different proteases to a degree of hydrolysis of between 15 and 35% without adjusting the pH during hydrolysis to produce a hydrolyzed slurry, inactivating the proteases and separating the hydrolyzed slurry with an ultrafiltration unit having a cut-off value above 5,000 to form a permeate containing the vegetable protein hydrolyzate. One protease may be obtained from B. Licheniformis and the other from B. Subtilis. The hydrolyzed slurry or the permeate may be treated with activated carbon, and the permeate may be concentrated by nanofiltration and/or by evaporation.

    摘要翻译: 通过使用非pH值水解和超滤的组合的方法,以高产率生产出品尝和感官可接受的植物蛋白水解产物如大豆,豌豆或米蛋白水解产物。 优选地,通过将​​含有至少65%植物蛋白作为干物质的材料和水混合以形成含有约7-20%的植物蛋白质含量的浆料,将浆料加热至60℃以上,调节 将浆料的pH调节至约8.5,用至少两种不同蛋白酶将浆料水解至15至35%之间的水解度,而不调节水解期间的pH以产生水解浆液,使蛋白酶失活并将水解的浆液与 具有超过5000的截止值的超滤单元以形成含有植物蛋白水解产物的渗透物。 一种蛋白酶可以从地衣芽孢杆菌获得,另一种来自枯草芽孢杆菌。 可以用活性炭处理水解的浆液或渗透物,并且可以通过纳滤和/或通过蒸发浓缩渗透物。