中科微点-全球专利检索

  1. Login
  2. Sign Up

Search Results

1992 records (took 0.028 seconds)

    METHOD FOR PROCESSING FISCHER-TROPSCH OFF-GAS
    84.
    发明申请
    METHOD FOR PROCESSING FISCHER-TROPSCH OFF-GAS 有权
    用于处理截流阀的方法

    公开(公告)号：US20150336043A1

    公开(公告)日：2015-11-26

    申请号：US14758452

    申请日：2013-12-31

    Applicant: SHELL OIL COMPANY

    Inventor： Sivakumar SADASIVAN VIJAYAKUMARI

    IPC: B01D53/047 ,  C01B31/18 ,  C10G2/00 ,  C01B31/20

    CPC classification number: B01D53/047 ,  B01D2253/102 ,  B01D2253/104 ,  B01D2253/106 ,  B01D2253/108 ,  B01D2253/116 ,  B01D2256/10 ,  B01D2256/16 ,  B01D2256/20 ,  B01D2256/245 ,  B01D2257/502 ,  B01D2257/504 ,  B01D2259/40071 ,  B01J20/08 ,  B01J20/103 ,  B01J20/18 ,  B01J20/20 ,  B01J2220/42 ,  B01J2220/606 ,  C01B3/56 ,  C01B32/40 ,  C01B32/50 ,  C10G2/32 ,  C10K1/32 ,  Y02C10/08 ,  Y02P20/152

    Abstract: This invention concerns a method for recovering carbon monoxide and carbon dioxide from Fischer-Tropsch off-gas by feeding Fischer-Tropsch off-gas through a column comprising an adsorbent bed, and discharging effluent, optionally rinsing the column and the adsorbent bed by feeding NG and discharging effluent until at least 60% of the carbon monoxide that was present in the bed is discharged, pressurizing the column and adsorbent bed with NG, rinsing the column and the adsorbent bed by feeding NG until at least 50% of the carbon dioxide present at the commencement of this rinsing step is discharged, rinsing the column and adsorbent bed by feeding a mixture of hydrogen and nitrogen, pressurizing the column and adsorbent bed by feeding a mixture of hydrogen and nitrogen. With this method a feed comprising at least 50 vol % carbon monoxide can be produced. Furthermore, methane and carbon dioxide at a high pressure can be recovered from the Fischer-Tropsch gas. This can be fed to a gasifier or a reformer. In a preferred embodiment a gas comprising at least 80 vol % hydrogen is produced as well.

    Abstract translation: 本发明涉及一种从费 - 托废气中回收一氧化碳和二氧化碳的方法，该方法是通过将费 - 托废气通过包括吸附床的塔排出，排出流出物，任选地通过进料NG漂洗该柱和吸附剂床 并排出流出物直到存在于床中的一氧化碳的至少60％排出，用NG加压柱和吸附剂床，通过进料NG冲洗柱和吸附床，直至存在至少50％的二氧化碳 在该冲洗步骤开始时排出，通过供给氢和氮的混合物冲洗柱和吸附剂床，通过供给氢和氮的混合物来加压塔和吸附剂床。 使用该方法可以生产包含至少50体积％一氧化碳的进料。 此外，可以从费 - 托气体回收高压下的甲烷和二氧化碳。 这可以被供给到气化器或重整器。 在优选的实施方案中，也产生包含至少80体积％的氢的气体。

    Process for preparing ball-type desulfurizer with high sulfur capacity and product thereof
    87.
    发明授权
    Process for preparing ball-type desulfurizer with high sulfur capacity and product thereof 有权
    具有高硫容量的球型脱硫剂及其制品的制备方法

    公开(公告)号：US09149792B2

    公开(公告)日：2015-10-06

    申请号：US14122536

    申请日：2012-05-21

    Applicant: Tong Zhou ,  Gang Zhao ,  Fujiang Hong ,  Wenjun Mao ,  Qunyang Gao ,  Bingyi Li

    Inventor： Tong Zhou ,  Gang Zhao ,  Fujiang Hong ,  Wenjun Mao ,  Qunyang Gao ,  Bingyi Li

    IPC: B01J20/06 ,  B01J20/08 ,  B01J20/30 ,  B01D53/50 ,  B01J20/28 ,  B01J20/10 ,  C01G49/02 ,  B01J20/02 ,  B01J20/32

    CPC classification number: B01J20/3078 ,  B01D53/508 ,  B01D2253/102 ,  B01D2253/1124 ,  B01D2253/304 ,  B01D2255/20738 ,  B01J20/0229 ,  B01J20/06 ,  B01J20/08 ,  B01J20/106 ,  B01J20/28004 ,  B01J20/28019 ,  B01J20/2803 ,  B01J20/28042 ,  B01J20/3028 ,  B01J20/3042 ,  B01J20/32 ,  B01J20/3204 ,  B01J20/3212 ,  B01J20/3236 ,  B01J20/324 ,  B01J20/3293 ,  C01G49/02

    Abstract: The present invention provides a process for preparing ball-type desulfurizer with high sulfur capacity, comprising the following steps: placing initial balls in a rolling equipment; wetting the surface of the initial balls with an aqueous solution of an organic binder; then alternately adding non-crystalline iron oxide hydroxide and the aqueous solution of the organic binder to gradually form small balls of non-crystalline iron oxide hydroxide with high sulfur capacity and different diameters; and adjusting the shape of the small balls and then roasting or naturally drying the small balls. In the desulfurizer prepared by this method, the initial balls constitutes 0.98 wt %-9.03 wt % of the desulfurizer, the non-crystalline iron oxide hydroxide constitutes 90.29 wt %-98.62 wt % of the desulfurizer, and the organic binder constitutes 0.58 wt %-0.89 wt % of the desulfurizer. The present invention solves the problems that the desulfurizer with high sulfur capacity in the prior art has a high binder content and poor water resistance and diffusion performance, and provides a process for preparing a desulfurizer with high sulfur capacity, wherein a desulfurizer with high sulfur capacity and low binder content, good water resistance, good diffusion performance can be prepared.

    Abstract translation: 本发明提供了一种制备具有高硫容量的球型脱硫剂的方法，包括以下步骤：将初始球放置在轧制设备中; 用有机粘合剂的水溶液润湿初始球的表面; 然后交替加入非晶态铁氧化物氢氧化物和有机粘合剂水溶液逐渐形成具有高硫容量和不同直径的非结晶铁氧化物氢氧化物的小球; 并调整小球的形状，然后焙烧或自然干燥小球。 在通过该方法制备的脱硫剂中，初始球构成脱硫剂的0.98重量％〜0.03重量％，非结晶性氧化铁氢氧化物构成脱硫剂的90.29重量％-98.62重量％，有机粘合剂占0.58重量％ -0.89重量％的脱硫剂。 本发明解决现有技术中具有高硫容量的脱硫剂具有高粘合剂含量和差的耐水性和扩散性能的问题，并且提供了具有高硫容量的脱硫剂的制备方法，其中具有高硫容量的脱硫剂 粘合剂含量低，耐水性好，扩散性能好。

Patent Agency Ranking