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    • 3. 发明授权
    • Tow of melt-spun filaments
    • 熔纺丝
    • US5804303A
    • 1998-09-08
    • US826270
    • 1997-03-27
    • Jurgen LorenzAxel Vischer
    • Jurgen LorenzAxel Vischer
    • D06B1/02D02G1/12D06C7/00D06C7/02D02G3/00
    • D02G1/12Y10T428/29Y10T428/2909
    • A tow of melt spun filaments and a method for treating such filaments to produce a tow of uniformly crimped filaments having a high initial modulus by heat setting and stuffer box crimping includes the steps of heat-setting the tow, spraying the hot-heat-set tow with an aqueous fiber finish to effect shocklike cooling of the tow, passing the sprayed tow to a pair of squeeze rolls in whose nip it is kneaded through using a defined nip pressure and squeezed off to a fiber finish pickup of 0.7 to 7% by weight of the tow weight, heating the squeezed-off moist tow on a heated multiroll arrangement in such a way that it leaves the multiroll arrangement with a moisture content of 0.5 to 5% by weight of the tow weight and a temperature of 40.degree. to 1000.degree. C., feeding the tow with this moisture content and this temperature to a crimping machine and crimping it.
    • 一丝熔融纺丝长丝和一种用于处理这种长丝以通过热定形和填塞箱卷曲产生具有高初始模量的均匀卷曲长丝的丝束的方法包括热定型丝束的步骤,喷涂热定型 用水性纤维整理剂牵引以实现丝束的冲击式冷却,将喷射的丝束通过使用限定的辊隙压力捏合的一对挤压辊,并将其挤压至0.7至7%的纤维终点拾取,通过 将丝束重量的重量加热到加热的多辊装置上,使得其以多重卷轴布置的方式加热挤出的湿丝,其含水量为丝束重量的0.5至5重量%,温度为40℃至 将该水分含量的丝束和该温度送入压接机并压接。
    • 4. 发明授权
    • Process of treating a tow of melt-spun filaments
    • 处理熔纺纤维丝束的方法
    • US5679300A
    • 1997-10-21
    • US657804
    • 1996-05-31
    • Jurgen LorenzAxel Vischer
    • Jurgen LorenzAxel Vischer
    • D06B1/02D02G1/12D06C7/00D06C7/02D01D5/12
    • D02G1/12Y10T428/29Y10T428/2909
    • A method for treating a tow of melt-spun filaments to produce a tow of uniformly crimped filaments having a high initial modulus by heat-setting and stuffer box crimping includes the steps of heat-setting the tow, spraying the hot-heat-set tow with an aqueous fiber finish to effect shocklike cooling of the tow, passing the sprayed tow to a pair of squeeze rolls in whose nip it is kneaded through using a defined nip pressure and squeezed off to a fiber finish pickup of 0.7 to 7% by weight of the tow weight, heating the squeezed-off moist tow on a heated multiroll arrangement in such a way that it leaves the multiroll arrangement with a moisture content of 0.5 to 5% by weight of the tow weight and a temperature of 40.degree. to 100.degree. C., feeding the tow with this moisture content and this temperature to a crimping machine and crimping it.
    • 一种用于处理熔纺丝的丝束以通过热定形和填塞箱卷曲产生具有高初始模量的均匀卷曲长丝的丝束的方法包括以下步骤:将丝束热定型,喷射热热凝固丝束 具有水性纤维整理剂以实现丝束的冲击式冷却,将喷射的丝束通过使用限定的辊隙压力捏合的一对挤压辊,并挤压至0.7至7重量%的纤维终点拾取 的拖曳重量,加热挤压的湿拖曳在加热的多辊装置上,使得其离开多辊装置,水分含量为丝束重量的0.5至5重量%,温度为40至100℃ 将该水分含量和该温度的丝束供给到压接机并压接。
    • 5. 发明授权
    • Biological dephosphatization and (de)nitrification
    • 生物脱磷和(脱)硝化
    • US5252214A
    • 1993-10-12
    • US829463
    • 1992-01-31
    • Gunter LorenzJurgen Lorenz
    • Gunter LorenzJurgen Lorenz
    • C02F3/12C02F3/30
    • C02F3/1215C02F3/308Y02W10/15Y10S210/903Y10S210/906
    • A modified activated sludge system is provided wherein wastewater is treated to reduce BOD, nitrogen, and/or phosphorus. The disclosed system features a zone sequence nitrification/denitrification, with nitrification induced by recycling mixed liquor that contains a significant concentration of oxygen and nitrifying bacteria. With a further modification, the main treatment zones of the treatment system are split into two or more parallel treatment trains that are either high-loaded with BOD or low-loaded with BOD. The high-loaded sections facilitate the sludge generation and BOD removal, while the low-loaded sections are operated for nitrification and to enhance the growth of nitrifying bacteria. The parallel treatment zones combine and pass into a final denitrification zone. Phosphorus removal is achieved with phosphate release in a reverse flow regime to the main treatment, and phosphate retention primarily in aerated treatment zones in the main stream of the process. The phosphorus is discarded from the system as sludge.
    • 提供了改进的活性污泥系统,其中处理废水以减少BOD,氮和/或磷。 所公开的系统具有区域序列硝化/反硝化作用,通过回收含有显着浓度的氧气和硝化细菌的混合液引起的硝化作用。 经过进一步的修改,处理系统的主要处理区被分为两个或更多个平行的待处理列车,这些列车高负载BOD或低负载BOD。 高负荷部分有助于污泥生成和BOD去除,而低负荷部分用于硝化作用并且增强硝化细菌的生长。 平行处理区域结合并进入最终脱氮区。 在主要处理的反向流动状态下,通过磷酸盐释放实现磷去除,主要在主要流程中的充气处理区中进行磷酸盐保留。 磷作为污泥从系统中排出。
    • 7. 发明授权
    • Biological dephosphatization and (de)nitrification
    • 生物脱磷和(脱)硝化
    • US5344562A
    • 1994-09-06
    • US25946
    • 1993-03-03
    • Gunter LorenzJurgen Lorenz
    • Gunter LorenzJurgen Lorenz
    • C02F3/12C02F3/30
    • C02F3/1215C02F3/308Y02W10/15Y10S210/903Y10S210/906
    • A modified activated sludge system is provided wherein wastewater is treated to reduce BOD, nitrogen, and/or phosphorus. The disclosed system features a zone sequence nitrification/denitrification, with nitrification induced by recycling mixed liquor that contains a significant concentration of oxygen and nitrifying bacteria. With a further modification, the main treatment zones of the treatment system are split into two or more parallel treatment trains that are either high-loaded with BOD or low-loaded with BOD. The high-loaded sections facilitate the sludge generation and BOD removal, while the low-loaded sections are operated for nitrification and to enhance the growth of nitrifying bacteria. The parallel treatment zones combine and pass into a final denitrification zone. Phosphorus removal is achieved with phosphate release in a reverse flow regime to the main treatment, and phosphate retention primarily in aerated treatment zones in the main stream of the process. The phosphorus is discarded from the system as sludge.
    • 提供了改进的活性污泥系统,其中处理废水以减少BOD,氮和/或磷。 所公开的系统具有区域序列硝化/反硝化作用,通过回收含有显着浓度的氧气和硝化细菌的混合液引起的硝化作用。 经过进一步的修改,处理系统的主要处理区被分为两个或更多个平行的待处理列车,这些列车高负载BOD或低负载BOD。 高负荷部分有助于污泥生成和BOD去除,而低负荷部分用于硝化作用并且增强硝化细菌的生长。 平行处理区域结合并进入最终脱氮区。 在主要处理的反向流动状态下,通过磷酸盐释放实现磷去除,主要在主要流程中的充气处理区中进行磷酸盐保留。 磷作为污泥从系统中排出。
    • 8. 发明授权
    • Filtration of a liquid
    • 过滤液体
    • US4077880A
    • 1978-03-07
    • US507976
    • 1974-09-20
    • Jurgen LorenzFrank Mehdorn
    • Jurgen LorenzFrank Mehdorn
    • B01D35/02B01D35/28B01D37/00D01D1/10
    • B01D24/14B01D35/28
    • A process for filtering a liquid through a combination of a first sieve, a sand pack and a second sieve in the direction of flow of the liquid, is described. This process differs from the known process in that the liquid passes through a filter pack in which the mesh width of the first sieve is at most equal to the mesh width of the second sieve, and the mesh width of the second sieve is smaller than the smallest particle size of the sand in the sand pack. Furthermore, the mesh width of the second sieve is at most 80 microns.When using this process uniform filaments without variations in titer from filament to filament or over the length of a filament are obtained. The rise in pressure relating to time is very small.
    • 描述了通过第一筛,沙包和第二筛的组合在液体流动方向上过滤液体的方法。 该方法与已知的方法不同之处在于,液体通过第一筛网的筛网宽度等于第二筛网孔宽度的滤袋,第二筛网的筛网宽度小于 砂包中砂的最小粒径。 此外,第二筛的网孔宽度最多为80微米。