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    • 53. 发明申请
    • Dicarboxylic Acid Production with Self-Fuel Oxidative Destruction
    • 自燃氧化破坏的二羧酸生产
    • US20100113824A1
    • 2010-05-06
    • US12556099
    • 2009-09-09
    • Raymond Elbert Fogle, IIIRonald Buford SheppardTimothy Alan UpshawAlan George Wonders
    • Raymond Elbert Fogle, IIIRonald Buford SheppardTimothy Alan UpshawAlan George Wonders
    • C07C51/16
    • C07C51/265C07C63/26C07C63/15
    • The invention provides improved energy content in and shaft power recovery from off-gas from xylene oxidation reactions while at the same time minimizing wastewater treatment cost. More shaft power is produced using off-gas than is required to drive the main air compressor, even with preferred, relatively low oxidation temperatures. Simultaneously, an amount of wastewater greater than byproduct water from oxidation of xylene is kept in vapor form and treated along with off-gas pollutants in a self-sustaining (self-fueling) gas-phase thermal oxidative destruction unit. Optionally, off-gas is combined from multiple xylene oxidation reactors, comprising primary and/or secondary oxidation reactors and forming TPA and/or IPA. Optionally, air compressor condensate and caustic scrubber blowdown are used in a TPA process or as utility water, effectively eliminating normal flow of liquid wastewater effluent from a TPA plant. Optionally, PET off-gas containing the water of PET formation is treated in a shared thermal oxidative destruction unit, effectively eliminating normal flow of liquid wastewater effluent from a combined pX-to-TPA-to-PET plant.
    • 本发明提供了来自二甲苯氧化反应的废气的改进的能量含量和轴功率回收,同时使废水处理成本最小化。 即使使用优选的相对低的氧化温度,也可以使用除了驱动主空气压缩机所需的废气以外的更多的轴功率。 同时,大量来自二氧化碳氧化的副产物水的废水保持蒸气形式,并在自持(自燃)气相热氧化破坏装置中与废气污染物一起处理。 任选地,废气从包括初级和/或二级氧化反应器并形成TPA和/或IPA的多个二甲苯氧化反应器组合。 任选地,空气压缩机冷凝物和苛性碱洗涤器排污用于TPA方法或作为效用水,有效地消除了来自TPA设备的液体废水流出物的正常流动。 任选地,在共同的热氧化破坏单元中处理含有PET形成水的PET废气,有效地消除了从组合的pX到TPA到PET植物的液体废水流出物的正常流动。
    • 54. 发明申请
    • INTEGRATED STEAM HEATING IN POLYESTER PRODUCTION PROCESS
    • 聚酯生产过程中的一体化蒸汽加热
    • US20100113736A1
    • 2010-05-06
    • US12558003
    • 2009-09-11
    • Alan George WondersJames Donald SimpsonBruce Roger DeBruin
    • Alan George WondersJames Donald SimpsonBruce Roger DeBruin
    • C08G63/127
    • C08G63/78Y02P20/125
    • Integrated processes for making polyesters are disclosed, that include the steps of: (a) producing an aromatic polycarboxylic acid in a monomer production facility; (b) producing a polyester in a polyester production facility, wherein the producing of the polyester comprises the substeps of: (i) forming a polyester reaction medium comprising at least a portion of the aromatic polycarboxylic acid from the monomer production facility, (ii) subjecting at least a portion of the polyester reaction medium to one or more chemical reactions to thereby produce the polyester, (iii) heating the polyester reaction medium at one or more locations in the polyester production facility via indirect heat exchange with high-pressure steam, wherein the heating causes at least a portion of the high-pressure steam to condense and thereby provide pressurized condensed water, and (iv) flashing at least a portion of the pressurized condensed water to thereby produce lower-pressure steam; and (c) using at least a portion of the lower-pressure steam to provide thermal energy to the monomer production facility.
    • 公开了制造聚酯的综合方法,包括以下步骤:(a)在单体生产设备中制备芳族多元羧酸; (b)在聚酯制造设备中制造聚酯,其中聚酯的制造包括以下子步骤:(i)从单体生产设备形成包含至少一部分芳族多元羧酸的聚酯反应介质,(ii) 使聚酯反应介质的至少一部分进行一个或多个化学反应从而生产聚酯,(iii)通过与高压蒸汽的间接热交换在聚酯生产设备中的一个或多个位置处加热聚酯反应介质, 其中所述加热使得所述高压蒸汽的至少一部分冷凝,从而提供加压的冷凝水,和(iv)使加压冷凝水的至少一部分闪蒸,从而产生低压蒸汽; 和(c)使用至少一部分低压蒸汽来向单体生产设备提供热能。