Process and system for converting plastics waste into oil
    1.
    发明授权
    Process and system for converting plastics waste into oil 失效
    将塑料废物转化为油的工艺和制度

    公开(公告)号:US6107532A

    公开(公告)日:2000-08-22

    申请号:US57725

    申请日:1998-04-09

    CPC分类号: C10G1/10

    摘要: Disclosed is an economical process for treating a large amount of plastics waste in which thermoplastics, crosslinked plastics, thermosetting plastics or a mixture thereof can be continuously and rapidly degraded and converted into oil without sorting various types of plastics waste. According to this process, powdered plastics obtained by grinding thermoplastics, crosslinked plastics, thermosetting plastics or a mixture thereof is mixed with water to form a slurry, and a dispersing agent such as a water-absorbing resin, a water-soluble polymer or a surface-active agent is added thereto. The resulting mixed slurry is fed to a tubular continuous reactor where the powdered plastics is degraded under reaction conditions causing the water to be in or near its supercritical region. Finally, oil is recovered from the reaction product.

    摘要翻译: 公开了一种用于处理大量塑料废料的经济方法,其中热塑性塑料,交联塑料,热固性塑料或其混合物可以连续且快速地降解并转化成油而不分类各种塑料废料。 根据该方法,将通过研磨热塑性塑料,交联塑料,热固性塑料或其混合物获得的粉末状塑料与水混合以形成浆料,并将分散剂如吸水树脂,水溶性聚合物或表面 添加活性剂。 将所得混合浆料进料到管状连续反应器中,其中粉末状塑料在引起水处于或接近其超临界区域的反应条件下降解。 最后,从反应产物中回收油。

    Exhaust gas desulfurizing method and system therefor
    5.
    发明授权
    Exhaust gas desulfurizing method and system therefor 有权
    废气脱硫方法及其系统

    公开(公告)号:US06656440B2

    公开(公告)日:2003-12-02

    申请号:US09914778

    申请日:2001-09-05

    IPC分类号: B01D5350

    摘要: A method and system for desulfurizing flue gas in which desulfurization is effected by bringing absorbent slurry containing limestone into contact with flue gas. The method classifies absorbent slurry extracted from a desulfurization absorber, returns a fine-side fluid to the desulfurization absorber, and sends a coarse-side fluid to a solid-liquid separator. Supplied limestone powder is mixed to yield limestone slurry by a solid-liquid mixer, and the limestone slurry is classified, sending the small-particle fluid component thereof to the desulfurization absorber, and sending the large-particle fluid component thereof to a limestone fine grinder. And, limestone contained in the large-particle fluid component is finely ground by the limestone fine grinder and the finely ground limestone is sent to the desulfurization absorber. According to the desulfurization method and system, the concentration of limestone in the desulfurization absorber is increased while the concentration of residual limestone in by-product gypsum is kept low, whereby the desulfurization performance of the absorber can be enhanced, and the operation power for the whole system can be decreased.

    摘要翻译: 通过使含有石灰石的吸收剂浆料与烟气接触来进行脱硫的脱硫烟道气的方法和系统。 该方法将从脱硫吸收器中提取的吸收剂浆料分类,将细边流体返回到脱硫吸收器,并将粗侧流体送至固液分离器。 将供给的石灰石粉末通过固液混合器混合,得到石灰石浆料,将石灰石浆料分级,将其中的小粒子流体成分送入脱硫吸收塔,将大颗粒流体成分送入石灰石细磨 。 并且,大颗粒流体组分中所含的石灰石由石灰石细研磨机精细研磨,精细研磨的石灰石被送到脱硫吸收器。 根据脱硫方法和系统,脱硫吸收剂中石灰石的浓度增加,副产物石膏中残留石灰石的浓度降低,吸收剂的脱硫性能可以提高, 整个系统可以减少。

    Flue gas treatment system
    7.
    发明授权
    Flue gas treatment system 失效
    烟气处理系统

    公开(公告)号:US5756052A

    公开(公告)日:1998-05-26

    申请号:US769633

    申请日:1996-12-18

    CPC分类号: B01D53/64 B01D53/501

    摘要: A flue gas treatment system is provided for which is capable of easily treating Se contained in flue gas, comprising an extractor 13 for extracting soluble components in the dust removed by a dry-type dust precipitator 5 into water to slurry the dust; insolubilizer supply 16 for supplying an insolubilizer for insolubilizing at least tetravalent Se to the dust slurry which has been slurried from the dust by the extractor 13; adsorbent supply 14 for supplying an adsorbent composed of an organism material for adsorbing at least hexavalent Se in the dust slurry; and separator 15 for solid-liquid separating the dust slurry to which the insolubilizer and the adsorbent have been supplied by said supplies.

    摘要翻译: 提供一种能够容易地处理烟气中所含的Se的烟道气处理系统,包括:将由干式除尘器5除去的粉尘中的可溶性成分提取到水中以将粉尘淤浆的提取器13; 用于供给用于使至少四价硒不溶解到由提取器13从灰尘中排出的粉尘浆料的不溶物供给装置16; 用于供给由用于吸附至少六价铬的生物材料组成的吸附剂的吸附剂供给装置14; 以及分离器15,用于固体分离由所述供给物供应的不溶化物和吸附剂的粉尘浆料。

    Wet exhaust gas desulfurization apparatus and method
    8.
    发明授权
    Wet exhaust gas desulfurization apparatus and method 失效
    湿法除气除气装置及方法

    公开(公告)号:US5221298A

    公开(公告)日:1993-06-22

    申请号:US827216

    申请日:1992-01-30

    IPC分类号: B01D53/50

    CPC分类号: B01D53/504 B01D53/501

    摘要: A wet exhaust gas desulfurization apparatus includes a housing, an absorbing solution (3, B) stored in the lower portion of the housing, a flue (1, 2, 11, 12, 21, 25) above the surface of the absorbing solution, and a partition plate (4, 15, 25) for dividing the flue into gas inlet and outlet portions. Exhaust gas is introduced as an untreated combustion gas from a space above an absorbing solution (3) divided by a partition plate (4) into the wet exhaust gas desulfurization apparatus, the lower edge (5) of the partition plate is immersed in the solution, pressure of the exhaust gas lowers the upper level (6) of the solution on the upper side of the plate to a level (6') through which the gas passes and flows under the partition plate in contact with the solution leaving the solution on the other side of the plate and then discharges through a space above the absorbing solution on the other side of the partition plate. The plate may be raised and lowered by a rack (4') and pinion ( 4") device, and water jet devices (29) may be used to wash absorbing solution off the surfaces (27, 28) of the plate continuously or intermittently.

    Method for treating waste gas to separate and recover gypsum and dust
therein
    9.
    发明授权
    Method for treating waste gas to separate and recover gypsum and dust therein 失效
    处理废气以分离和回收其中的石膏和粉尘的方法

    公开(公告)号:US4632810A

    公开(公告)日:1986-12-30

    申请号:US706117

    申请日:1985-02-27

    CPC分类号: C01F11/464 B01D53/501

    摘要: The present invention is directed to a method for treating a waste gas to separate and recover gypsum and a dust therein, characterized by comprising the steps of causing the waste gas to pass through a dry dust collector; introducing the gas into a gas absorber, in which a slurry containing at least one of calcium hydroxide or calcium carbonate as an absorbent is employed to remove SO.sub.2 and the dust passed through the dry dust collector from the waste gas; blowing air into the resultant absorbing liquid in the gas absorber to oxidize the absorbing liquid and to thereby produce gypsum; delivering them to an absorbing liquid tank, in which the slurry mainly containing the gypsum grains is separated from the other slurry mainly containing the dust by partition walls disposed therein; and directly taking out the respective slurries separately from the absorbing liquid tank.

    摘要翻译: 本发明涉及一种处理废气以分离和回收石膏和其中的灰尘的方法,其特征在于包括使废气通过干式除尘器的步骤; 将气体引入气体吸收器中,其中使用含有氢氧化钙或碳酸钙中的至少一种作为吸收剂的浆料来从废气中除去SO 2和通过干式集尘器的粉尘; 将空气吹送到吸收剂中的所得吸收液体中以氧化吸收液体,从而产生石膏; 将其输送到吸收液体罐中,其中主要含有石膏颗粒的浆料与主要由灰尘组成的其它浆料与设置在其中的分隔壁分离; 并直接从吸收液体罐中取出各自的浆料。

    Flue gas treating system and process
    10.
    发明授权
    Flue gas treating system and process 有权
    烟气处理系统及工艺

    公开(公告)号:US06863875B1

    公开(公告)日:2005-03-08

    申请号:US09658928

    申请日:2000-09-11

    IPC分类号: B01D53/60 C01B17/96

    CPC分类号: B01D53/60 B01D53/77

    摘要: In a flue gas treating system, an absorption tower (21), a reheating section (22) and a fan (23) are arranged in line on a vertical axis so as to function as at least a part of a stack for emitting the treated flue gas into the atmosphere. Moreover, in a flue gas treating process, the amount of ammonia injected in the denitration step (a denitrator (2)) and/or the amount of ammonia at a point downstream of the denitration step are determined so as to be on such an excessive level that ammonia or ammonium salt will remain in the flue gas introduced into the desulfurization step (absorption tower (21)). Thus, the size and cost of the equipment can be reduced.

    摘要翻译: 在烟道气处理系统中,吸收塔(21),再加热部分(22)和风扇(23)在垂直轴线上排成一列,以起到堆叠的至少一部分的作用, 烟气进入大气。 此外,在烟道气处理工序中,确定脱硝工序中注入的氨的数量(脱硝装置(2))和/或在脱硝工序的下游一点处的氨的量为过度 使得氨或铵盐保留在引入脱硫步骤(吸收塔(21))的烟道气中。 因此,可以减少设备的尺寸和成本。