Pumpable aqueous slurries of sewage sludge
    1.
    发明授权
    Pumpable aqueous slurries of sewage sludge 失效
    可排水污泥的含水浆料

    公开(公告)号:US5356540A

    公开(公告)日:1994-10-18

    申请号:US702579

    申请日:1991-05-20

    CPC classification number: C02F11/14 C02F11/06 C10L1/328 Y02W10/40

    Abstract: A pumpable aqueous slurry of sewage sludge as produced by the steps of (1) dewatering sewage sludge to produce an aqueous slurry having a solids content of about 10 to 25 wt. %; (2) pretreating said aqueous slurry of sewage sludge to improve its slurrying characteristics by one or a combination of (a) heating, (b) hydrothermal treatment, and (c) heating, mixing and shearing; and (3) mixing the following materials together at a temperature in the range of about ambient to 400.degree. F. to produce a pumpable aqueous slurry having a solids content in the range of about 30 to 65 wt. %: (a) pretreated aqueous slurry of sewage sludge; (b) a nonionic water soluble alkoxylated alkylphenol additive; and (c) sewage sludge-containing material and/or solid carbonaceous fuel-containing material to increase the solids loading.

    Abstract translation: (1)将污水污泥脱水以产生固体含量为约10至25重量%的含水浆料产生的下水污泥的可泵送含水浆料。 %; (2)通过(a)加热,(b)水热处理和(c)加热,混合和剪切的一种或组合来预处理所述污水污泥的所述含水浆料以改善其浆化特性; 和(3)在约环境温度至400°F的温度范围内将以下材料混合在一起,以产生固体含量在约30至65重量%范围内的可泵送含水浆料。 %:(a)污水污泥预处理水泥浆; (b)非离子水溶性烷氧基化烷基酚添加剂; 和(c)含污泥的材料和/或固体含碳燃料的材料以增加固体负载量。

    Process for disposing of sewage sludge
    2.
    发明授权
    Process for disposing of sewage sludge 失效
    处理污水污泥的处理方法

    公开(公告)号:US5292442A

    公开(公告)日:1994-03-08

    申请号:US955007

    申请日:1992-10-01

    Abstract: A process for disposing of sanitary sewage sludge by producing a pumpable slurry of sewage sludge with or without solid carbonaceous fuel and burning said slurry as fuel in a partial oxidation gas generator, furnace, or boiler. The aqueous slurry of sewage sludge is concentrated by removing water by means of a conventional belt filter press, centrifuge, or hydroclone. The dewatered slurry of sewage sludge is heated by direct contact with steam while air and organic vapors are simultaneously removed, to reduce the pressure in the system; hydrothermally treated in two steps with indirect and direct heat exchange with steam; dewatered by flash evaporation and centrifuging; and burned with or without admixture with solid carbonaceous fuel in a partial oxidation gasifier, furnace, boiler, or incinerator to produce synthesis gas or a hot raw effluent gas stream. In a preferred embodiment, the effluent gas stream is cleaned and purified and non-contaminating ash and slag are separated. By this process, noxious sewage sludge may be disposed of without contaminating the environment. Synthesis gas, reducing gas, or fuel gas may be produced.

    Abstract translation: 通过生产具有或不具有固体碳质燃料的污水污泥的可泵送浆料并在所述部分氧化气体发生器,炉或锅炉中燃烧所述浆料作为燃料来处理生活污水污泥的方法。 通过传统的带式压滤机,离心机或水力旋流器除去水,污泥污泥的含水浆液被浓缩。 污水污泥的脱水浆液通过与蒸汽直接接触而加热,同时除去空气和有机蒸汽,以减少系统的压力; 在两个步骤中进行水热处理,间接和直接与蒸汽进行热交换; 通过闪蒸和离心脱水; 并且在部分氧化气化器,炉,锅炉或焚烧炉中与固体碳质燃料混合或不混合,以产生合成气或热的原始流出气流。 在一个优选的实施方案中,将废气流清洁和净化,并且将非污染灰和渣分离。 通过这个过程,可以处理有害污水污泥而不污染环境。 可以生产合成气体,还原气体或燃料气体。

    Disposal of sewage sludge
    3.
    发明授权
    Disposal of sewage sludge 失效
    处理污水污泥

    公开(公告)号:US5188739A

    公开(公告)日:1993-02-23

    申请号:US801326

    申请日:1991-12-02

    Abstract: A process for disposing of sanitary sewage sludge by producing a pumpable slurry of sewage sludge and solid carbonaceous fuel e.g. coal, petroleum coke, rubber. The slurry is burned as a fuel in a partial oxidation gas generator, furnace, or boiler. In the process, an aqueous slurry of sewage sludge is concentrated by removing water by means of a conventional belt filter press or presses. The dewatered slurry of sewage sludge is hydrothermally treated and cooled and depressurized. The viscosity of the slurry of sewage sludge is reduced to less than about 2000 centipoise by shearing. The sheared sewage sludge is then ground together with a solid carbonaceous fuel to produce a pumpable slurry which is burned with a free-oxygen containing gas in a partial oxidation gasifier, furnace, boiler, or incinerator to produce a hot raw effluent gas stream. In a preferred embodiment, the effluent gas stream is cleaned and purified and non-contaminating ash and slag are separated. By this process, noxious sewage sludge may be disposed of without contaminating the environment. By-product synthesis gas, reducing gas, or fuel gas may be produced.

    Abstract translation: 通过生产下水泥浆和固体碳质燃料的可泵送浆料来处理生活污水污泥的方法,例如 煤,石油焦,橡胶。 在部分氧化气体发生器,炉子或锅炉中,浆料作为燃料燃烧。 在此过程中,通过传统的带式压滤机或压力机将污水污泥的含水浆料除去水进行浓缩。 污水污泥的脱水浆液进行水热处理,冷却和减压。 污泥污泥的粘度通过剪切减少到约2000厘泊。 然后将剪切的污水污泥与固体碳质燃料一起研磨以产生可部分浆料,其在部分氧化气化器,炉,锅炉或焚烧炉中用含游离氧气气体燃烧,以产生热的原料流出气流。 在一个优选的实施方案中,将废气流清洁和净化,并且将非污染灰和渣分离。 通过这个过程,可以处理有害污水污泥而不污染环境。 可以生产副产物合成气,还原气体或燃料气体。

    Partial oxidation of partially liquified plastic materials
    4.
    发明授权
    Partial oxidation of partially liquified plastic materials 失效
    部分液化塑料材料的部分氧化

    公开(公告)号:US5534040A

    公开(公告)日:1996-07-09

    申请号:US415153

    申请日:1995-03-31

    Abstract: A process for upgrading plastic material containing inorganic filler or reinforcement material for use as feedstock in a partial oxidation gas generator for the production of raw synthesis gas, fuel gas, or reducing gas. The plastic material is granulated and partially liquefied by heating in a closed autoclave at a temperature in the range of about 400.degree. F. to 495.degree. F. and a pressure in the range of about 150 psig to 750 psig while the plastic material is in contact with a pumpable hydrocarbonaceous liquid solvent. A pumpable slurry is thereby produced comprising solubilized plastic, unsolubilized plastic, hydrocarbonaceous liquid solvent, separated inorganic material and unseparated inorganic material. After removing the separated inorganic material, the remainder of the slurry is then reacted by partial oxidation to produce said raw synthesis gas, fuel gas or reducing gas.

    Abstract translation: 一种用于升级含有无机填料或增强材料的塑料材料的方法,用作用于生产原料合成气,燃料气体或还原气体的部分氧化气体发生器中的原料。 塑料材料通过在封闭的高压釜中在约400°F至495°F的温度范围内加热并在约150psig至750psig范围内的压力下进行造粒和部分液化,同时塑料材料在 与可泵送的烃类液体溶剂接触。 由此生产包含溶解的塑料,未溶解的塑料,含烃液体溶剂,分离的无机材料和未分离的无机材料的可泵送浆料。 除去分离的无机材料后,剩余的浆料然后通过部分氧化反应生成所述原料合成气,燃料气体或还原气体。

    Hydrothermal treatment and partial oxidation of plastic materials
    5.
    发明授权
    Hydrothermal treatment and partial oxidation of plastic materials 失效
    水热处理和部分氧化塑料材料

    公开(公告)号:US5498827A

    公开(公告)日:1996-03-12

    申请号:US131366

    申请日:1993-10-04

    Abstract: A process for upgrading plastic material containing inorganic filler or reinforcement material for use as feedstock in partial oxidation gas generator for the production of raw synthesis gas, fuel gas, or reducing gas. The plastic material is granulated and mixed with water to produce the plastic sludge. The plastic sludge is preheated at a temperature in the range of about 350.degree. F. to 475.degree. F. in the absence of air in a closed system. The preheated plastic sludge is then hydrothermally treated at a temperature in the range of about 450.degree. F. to 650.degree. F. at a pressure in the range of about 100 to 1200 psig and above the vapor pressure of water at that temperature. The hydrothermally treated plastic sludge is cooled, degassed, and mixed with ground solid carbonaceous fuel, e.g., coal and water, to produce a pumpable aqueous slurry having a solids content in the range of about 40 to 60 wt. %. The pumpable aqueous slurry is then reacted by partial oxidation to produce said synthesis gas, fuel gas, or reducing gas. In one embodiment, a portion of coal is mixed with the plastic sludge prior to the aforesaid preheating and hydrothermal steps.

    Abstract translation: 一种用于升级含有无机填料或增强材料的塑料材料的方法,用作用于生产原料合成气,燃料气体或还原气体的部分氧化气体发生器中的原料。 塑料材料与水混合制成塑料污泥。 塑料污泥在封闭系统中不存在空气的情况下,在约350°F至475°F的温度范围内进行预热。 然后将预热的塑料污泥在约450-150°F范围内的温度下进行水热处理,压力范围为约100至1200psig,并高于该温度下水的蒸气压。 水热处理的塑料污泥被冷却,脱气并与研磨的固体碳质燃料例如煤和水混合,以产生固体含量在约40至60重量%范围内的可泵送水性浆料。 %。 然后可泵送的含水浆料通过部分氧化反应以产生所述合成气体,燃料气体或还原气体。 在一个实施方案中,在上述预热和水热步骤之前,将一部分煤与塑料污泥混合。

    Process for disposing of sewage sludge
    6.
    发明授权
    Process for disposing of sewage sludge 失效
    处理污水污泥的处理方法

    公开(公告)号:US5234469A

    公开(公告)日:1993-08-10

    申请号:US722819

    申请日:1991-06-28

    Abstract: A process for disposing of sewage sludge comprising the steps of, (1) dewatering the sewage sludge to produce an aqueous slurry of sewage sludge having a solids content of about 10 to 50 wt. %; (2) heating and mildly shearing said dewatered sewage sludge at about 150.degree. F. to 210.degree. F. in the absence of air for 3 seconds to 60 minutes by a rotor/mixer at a speed of about 15 to 1000 r.p.m., thereby producing a pumpable slurry having a viscosity of less than about 2500 centipoise; (3) mixing at a temperature in the range of about ambient to 200.degree. F. the slurry of sewage sludge from (2) with a supplemental fuel to produce a pumpable slurry of sewage sludge and supplemental fuel having a solids content in the range of about 50 to 65 wt. % and a higher heating value in the range of about 6,000 to 18,000 BTU/LB; and (4) burning said pumpable slurry from (3) in a partial oxidation gasifier, furnace, boiler, or incinerator to produce an effluent gas stream. In a preferred embodiment, the effluent gas stream is cleaned and purified and non-contaminating ash and slag are separated. By this process, noxious sewage sludge may be disposed of without contaminating the environment.

    Abstract translation: 一种处理污水污泥的方法,包括以下步骤:(1)将污水污泥脱水以产生固体含量为约10至50重量%的污水污泥的含水浆料。 %; (2)通过转子/混合器以大约15至1000rpm的速度在没有空气的情况下,在约150°F至210°F的温度下加热和温和地剪切所述脱水污水污泥3秒至60分钟,由此产生 具有小于约2500厘泊的粘度的可泵送浆料; (3)在约环境温度至200°F的温度范围内混合来自(2)的污水污泥与补充燃料的浆料,以产生污泥和可补充的燃料,其中固体含量范围为 约50至65wt。 在约6,000至18,000BTU / LB的范围内具有较高的热值; 和(4)在部分氧化气化器,炉,锅炉或焚烧炉中将来自(3)的可泵送浆料燃烧以产生流出气流。 在一个优选的实施方案中,将废气流清洁和净化,并且将非污染灰和渣分离。 通过这个过程,可以处理有害污水污泥而不污染环境。

    Partial oxidation of products of liquefaction of plastic materials
    7.
    发明授权
    Partial oxidation of products of liquefaction of plastic materials 失效
    塑料材料液化产物的部分氧化

    公开(公告)号:US5445659A

    公开(公告)日:1995-08-29

    申请号:US130922

    申请日:1993-10-04

    CPC classification number: C10G1/065 C10G1/006 C10G1/10 Y10S48/07

    Abstract: A process for converting scrap plastic material into a high quality transportation fuel. The plastic material is granulated and mixed with granulated solid carbonaceous fuel e.g. coal and liquid hydrocarbonaceous solvent e.g. waste motor oil to produce a plastic-containing sludge. The plastic-containing sludge is liquefied in a closed autoclave while in contact with hydrogen gas. A pumpable slurry from the autoclave is heated and fractionated in a fractionation zone to produce a hydrocarbonaceous distillate which may be used for transportation fuel. A bottoms stream from the fractionation zone comprising liquid hydrocarbonaceous material and inorganic material is reacted by partial oxidation to produce nontoxic slag and raw synthesis gas, fuel gas or reducing gas which may be purified in a gas purification zone.

    Abstract translation: 将废塑料材料转化为高质量运输燃料的方法。 将塑料材料造粒并与颗粒状固体碳质燃料混合。 煤和液体烃类溶剂如 废机油生产含塑料的污泥。 含有含塑料的污泥在与氢气接触的密闭高压釜中液化。 将来自高压釜的可泵送的浆料在分馏区中加热分馏,以产生可用于运输燃料的含烃馏出物。 来自包含液体含烃材料和无机材料的分馏区的塔底物流通过部分氧化反应,生成无毒渣和生物合成气,燃气或还原气体,其可以在气体净化区中纯化。

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