Apparatus for continuous carbon dioxide absorption
    1.
    发明申请
    Apparatus for continuous carbon dioxide absorption 审中-公开
    连续二氧化碳吸收装置

    公开(公告)号:US20040250684A1

    公开(公告)日:2004-12-16

    申请号:US10491932

    申请日:2004-08-10

    IPC分类号: B01D053/14

    摘要: Apparatus for removing carbon dioxide from a stream of air or other gas, which includes a vertical gas absorption reactor containing loosely packed mixing units submerged in a carbon dioxide absorbent liquid; gas to be treated is admitted at or near this base of the rector, is broken into small bubbles by the mixing units, and passes through the absorbent liquid to remove a high percentage of carbon dioxide; treated gas leaves from the top of the reactor, a regenerator associated with the reactor continually or intermittently regenerates the absorbent liquid and is arranged to receive absorbent liquid to be treated through an outlet from the reactor which is located higher up the wall of the reactor than the inlet for returning treated liquid to the reactor.

    摘要翻译: 用于从空气或其它气体流中除去二氧化碳的装置,其包括垂直的气体吸收反应器,其包含浸没在二氧化碳吸收液体中的松散填充的混合单元; 要处理的气体在反应器底部或其附近进入,由混合单元破碎成小气泡,并通过吸收液体以除去高百分比的二氧化碳; 经反应器顶部处理的气体叶片,与反应器连接或间歇地再生吸收液体的再生器,并被布置成通过位于反应器壁上方的反应器的出口接收待处理的待吸收液体, 用于将经处理的液体返回到反应器的入口。

    Process for the removal of the hydrogen sulfide contained in natural gas
    2.
    发明申请
    Process for the removal of the hydrogen sulfide contained in natural gas 失效
    用于除去天然气中所含的硫化氢的方法

    公开(公告)号:US20040163537A1

    公开(公告)日:2004-08-26

    申请号:US10736850

    申请日:2003-12-17

    申请人: ENI S.p.A.

    IPC分类号: B01D053/14

    CPC分类号: C10L3/102 C10L3/10

    摘要: Process for the removal of the hydrogen sulfide contained in natural gas, which comprises: a. absorbing the hydrogen sulfide present in natural gas by means of a virgin naphtha, in an adsorbing device and with a molar ratio virgin naphtha/H2S ranging from 0.85 to 1.5; b. recovering the hydrogen sulfide absorbed by the virgin naphtha as head product of a distillation column operating with a reflux having a temperature of between null5 and null20null C.; c. recycling the virgin naphtha discharged as bottom product of the distillation column, to the absorption step (a); d. introducing the hydrogen sulfide back to the production field of natural gas, at the temperature and pressure conditions present at the head of the distillation column.

    摘要翻译: 用于除去天然气中所含的硫化氢的方法,其包括:a。 在吸附装置中以原始石脑油吸收存在于天然气中的硫化氢,在0.85至1.5之间的摩尔比的原始石脑油/ H 2 S; b。 回收由原始石脑油吸收的硫化氢作为温度在-5至-20℃的回流操作的蒸馏塔的头部产物; C。 将作为蒸馏塔的底部产物排出的原始石脑油循环到吸收步骤(a); d。 在存在于蒸馏塔头部的温度和压力条件下将硫化氢引入天然气生产领域。

    Method for the absorptive outward transfer of ammonia and methane out of synthesis gas
    3.
    发明申请
    Method for the absorptive outward transfer of ammonia and methane out of synthesis gas 失效
    合成气中氨和甲烷吸收向外转移的方法

    公开(公告)号:US20040139856A1

    公开(公告)日:2004-07-22

    申请号:US10473456

    申请日:2004-03-11

    IPC分类号: B01D053/14

    摘要: The invention relates to a process for the absorptive separation of NH3 and CH4 from a gas under high pressure, which at least contains NH3, H2, N2 and CH4, using a high-boiling, physically acting and regenerable solvent which contains homologues of alkylene glycol-alkyl-ether and which also may contain water, the absorbed components NH3, H2, N2 and CH4 being separated from the laden solvent in at least two further process steps at different pressure rates, thereby withdrawing at least one NH3-rich and at least one CH4-rich gas fraction from the solvent. This process is particularly suitable to be incorporated as unit in an ammonia production plant.

    摘要翻译: 本发明涉及一种用于高压气体吸收分离NH 3和CH 4的方法,该方法至少含有NH 3,H 2,N 2和CH 4,使用高沸点,物理作用和可再生的溶剂,其含有亚烷基二醇的同系物 - 烷基 - 醚,并且其还可以含有水,吸收的组分NH 3,H 2,N 2和CH 4在不同的压力速率下在至少两个另外的工艺步骤中从负载溶剂中分离,从而抽出至少一种富NH3,并且至少 来自溶剂的一种富含CH 4的气体馏分。 该方法特别适合作为单元并入氨生产设备中。

    CO2 recovery process for supercritical extraction
    4.
    发明申请
    CO2 recovery process for supercritical extraction 失效
    超临界萃取二氧化碳回收过程

    公开(公告)号:US20040118281A1

    公开(公告)日:2004-06-24

    申请号:US10671163

    申请日:2003-09-25

    IPC分类号: B01D053/14

    摘要: A carbon dioxide recovery apparatus and process for supercritical extraction includes providing a process stream from a supercritical extraction procedure in which the process stream includes pressurized carbon dioxide, extraction process waste and optionally at least one co-solvent; reducing the pressure of the process stream below critical pressure; venting low pressure carbon dioxide vapor to exhaust; cooling the process stream to form a two phase mixture; separating the two phase mixture into a process liquid, containing co-solvent if present, and a process vapor phase stream; collecting the process liquid; filtering the process vapor phase stream to remove particulates and optionally residual co-solvent; passing the filtered process vapor stream through an adsorber to remove trace impurities to form a purified carbon dioxide vapor stream; and, drying the purified carbon dioxide vapor stream to remove residual water vapor.

    摘要翻译: 二氧化碳回收装置和用于超临界萃取的方法包括提供来自超临界萃取方法的工艺流,其中工艺流包括加压二氧化碳,提取工艺废物和任选的至少一种共溶剂; 降低工艺流压力低于临界压力; 将低压二氧化碳蒸气排放到排气口; 冷却工艺流以形成两相混合物; 将两相混合物分离成含有共溶剂(如果存在)的工艺液体和工艺气相物流; 收集工艺液体; 过滤气相物流以除去微粒和任选的残余共溶剂; 使过滤的过程蒸汽流通过吸附器以除去痕量杂质以形成纯化的二氧化碳蒸汽流; 并干燥纯化的二氧化碳蒸气流以除去残留的水蒸汽。

    Foam detector and disruptor
    5.
    发明申请
    Foam detector and disruptor 有权
    泡沫探测器和破坏器

    公开(公告)号:US20040083892A1

    公开(公告)日:2004-05-06

    申请号:US10288391

    申请日:2002-11-05

    IPC分类号: B01D053/14

    摘要: An apparatus and method are disclosed to detect foam above a liquid sample in a sparge vessel, and disrupt any foam that may exist. The foam sensor includes an optical emitter and optical sensor coupled to a sparge vessel above the level of the liquid sample. Foam is detected if the light beam is attenuated or blocked. The foam disrupter provides thermal energy to raise the temperature of a surface in the sparge vessel to break up the foam, which may condense on the walls of the sparge vessel.

    摘要翻译: 公开了一种用于在喷射容器中检测液体样品上方的泡沫并破坏可能存在的任何泡沫的装置和方法。 泡沫传感器包括耦合到液体样品水平面上方的喷射容器的光发射器和光学传感器。 如果光束被衰减或阻挡,则检测到泡沫。 泡沫破碎器提供热能以提高喷射容器中的表面的温度以分解泡沫,泡沫可以在喷射容器的壁上冷凝。

    CATALYST ALLOWING CONVERSION OF NATURAL GAS HYDRATE AND LIQUID CO2 TO CO2 HYDRATE AND NATURAL GAS
    6.
    发明申请
    CATALYST ALLOWING CONVERSION OF NATURAL GAS HYDRATE AND LIQUID CO2 TO CO2 HYDRATE AND NATURAL GAS 有权
    催化剂允许天然气水合物和二氧化碳向二氧化碳和天然气转化

    公开(公告)号:US20040060438A1

    公开(公告)日:2004-04-01

    申请号:US10256132

    申请日:2002-09-27

    IPC分类号: B01D053/14

    摘要: A method for recovering large volumes of hydrocarbon fuels, particularly methane (CH4), using commercially available reagents which are strongly water-soluble and soluble in liquid CO2 in the presence of liquid CO2 injected into the methane hydrate formation. The reagents which are strongly water-soluble and soluble in liquid CO2 form dilute aqueous acids that significantly increase the rate of conversion of methane hydrate into methane and CO2 hydrate, thereby allowing the natural gas to be released in a form that can then be recovered in large quantities using conventional means. The preferred embodiment uses SO3, HCl or other strongly water soluble gas to cause the methane hydrate ice crystals to melt and form an aqueous solution. The aqueous solution contacts the methane hydrate ice on one side and liquid carbon dioxide on the other side. The system spontaneously adjusts so that the acid solution remains strong enough to melt the methane ice, but not strong enough to prevent the formation of the carbon dioxide ice at the recovery temperature and pressure. The natural gas is liberated from the hydrate and removed by conventional means.

    摘要翻译: 使用在注入到甲烷水合物层中的液态CO 2存在下,使用可溶于水并可溶于液体CO 2的市售试剂回收大量烃燃料,特别是甲烷(CH 4)的方法。 强溶于水和可溶于液态CO2的试剂形成稀酸水溶液,显着提高甲烷水合物转化为甲烷和二氧化碳水合物的转化率,从而使天然气以一种形式被释放, 大量使用常规手段。 优选的实施方案使用SO 3,HCl或其它强水溶性气体来使甲烷水合物冰晶体熔化并形成水溶液。 水溶液与一侧的甲烷水合物冰和另一侧的液体二氧化碳接触。 系统自发调节,使得酸溶液保持足够的强度以熔化甲烷冰,但不足以防止在回收温度和压力下形成二氧化碳冰。 天然气从水合物中释放并通过常规方法除去。

    Elimination process of fluorinated anionic surfactants
    7.
    发明申请
    Elimination process of fluorinated anionic surfactants 失效
    氟化阴离子表面活性剂的消除过程

    公开(公告)号:US20040016343A1

    公开(公告)日:2004-01-29

    申请号:US10620418

    申请日:2003-07-17

    IPC分类号: B01D053/14

    摘要: An elimination process of fluorinated anionic sufactants from exhausted gaseous streams, wherein the gaseous stream is put into contact with aqueous solutions having in the range from 3.5 to 13.8, the aqueous solution density being lower than 1.05 g/cm3, wherein the concentration in the aqueous solution of the fluorinated anionic surfactant removed by the gaseous stream is lower than or equal to 70 ppm.

    摘要翻译: 氟化阴离子表面活性剂从排出气流中的消除过程,其中气流与3.5〜13.8范围内的水溶液接触,水溶液密度低于1.05g / cm 3,其中浓度 在由气态物质除去的氟化阴离子表面活性剂的水溶液中低于或等于70ppm。

    Wet-process gas treatment method and wet-process gas treatment apparatus
    8.
    发明申请
    Wet-process gas treatment method and wet-process gas treatment apparatus 失效
    湿法气处理方法和湿法气处理装置

    公开(公告)号:US20030116018A1

    公开(公告)日:2003-06-26

    申请号:US10321482

    申请日:2002-12-18

    IPC分类号: B01D053/14

    摘要: In a wet-process gas treatment method of treating an acid gas by means of at least two treating columns connected in series, ratio of concentration of acid gas at an outlet to concentration of acid gas at an inlet, of a first treating column is set higher than ratio of concentration of acid gas at an outlet to concentration of acid gas at an inlet, of at least one of other treating columns, thereby preventing deposits from forming in the interior of connecting pipes between the columns and in the interiors of the treating columns, to prevent the connecting pipes from their blockage.

    摘要翻译: 在通过串联连接的至少两个处理塔处理酸性气体的湿法气体处理方法中,设定第一处理塔的出口处的酸性气体浓度与入口处的酸性气体浓度的比例 高于出口处的酸性气体浓度与入口处的酸性气体浓度的比例,至少其他处理塔中的一种处理塔中的至少一种,从而防止在管柱内部和处理室内部的连接管内部形成沉积物 柱,以防止连接管堵塞。

    Catalyst device for clarification of exhaust gas
    9.
    发明申请
    Catalyst device for clarification of exhaust gas 审中-公开
    用于澄清废气的催化剂装置

    公开(公告)号:US20020172625A1

    公开(公告)日:2002-11-21

    申请号:US10069596

    申请日:2002-07-08

    摘要: A catalytic apparatus for exhaust purification, provided in an exhaust path of an internal-combustion engine operable with at least a theoretical air-fuel ratio and a lean air-fuel ratio, is provided with a three-way catalyst (4) having an inner layer (12a) thereof mainly containing rhodium as a noble metal to be activated in an oxygen concentration lowering atmosphere and a surface layer (12b) thereof mainly containing platinum or palladium as a noble metal to be activated in an oxygen concentration increasing atmosphere. In the catalytic apparatus, platinum or palladium in the surface layer is activated in lean operation to perform an HC purifying function effectively. If oxygen is temporarily in short supply during the change from a lean air-fuel ratio of exhaust gas over to a stoichiometric air-fuel ratio, oxygen is supplemented to purify HC by utilizing the O2 storage function of platinum or palladium as the noble metal, whereby the HC purifying rate can be prevented from temporarily suddenly lowering. The catalytic apparatus for exhaust purification can secure satisfactory HC purifying performance even in a lean area without increasing the noble metal loading of the three-way catalyst, so that it can be manufactured at low cost.

    摘要翻译: 一种用于排气净化的催化装置,其设置在能够以至少理论空燃比和贫空燃比操作的内燃机的排气路径中,具有内部具有内燃机的三元催化剂(4) 其主要含有在氧浓度降低气氛中活化的贵金属的铑和主要含有铂或钯作为贵金属的表面层(12b)的层(12a),以在氧浓度增加的气氛中活化。 在催化装置中,表面层中的铂或钯在稀薄操作中被激活以有效地执行HC净化功能。 如果在从废气的稀薄空气 - 燃料比变化到化学计量空燃比的过程中,氧气暂时不足,则补充氧气,通过利用铂或钯作为贵金属的O2储存功能来净化HC, 从而可以防止HC净化率暂时突然降低。 用于排气净化的催化装置即使在稀薄区域也可以确保令人满意的HC净化性能,而不会增加三元催化剂的贵金属负载量,从而可以以低成本制造。