Method and apparatus for withdrawing solid catalyst particles
    141.
    发明授权
    Method and apparatus for withdrawing solid catalyst particles 失效
    用于提取固体催化剂颗粒的方法和装置

    公开(公告)号:US3654143A

    公开(公告)日:1972-04-04

    申请号:US3654143D

    申请日:1969-12-29

    CPC classification number: B01J8/0015 B01J8/0025 B01J8/004 B01J2208/00761

    Abstract: IN CATALYST IN A REACTION TANK HAVING A MATERIAL FEED PIPE AT THE LOWER PORTION THEREOF AND A PRODUCT-TAKINGOUT-PIPE AT THE UPPER PORTION THEREOF, A DISCHARGE NOZZLE AND A SUCTION NOZZLE ARE PROVIDED, THE DISCHARGE NOZZLE BEING CONNECTED TO THE DISCHARGE SIDE OF A PUMP PROVIDED OUTSIDE THE REACTION TANK AND THE SUCTION NOZZLE BEING CONNECTED TO THE SUCTION SIDE OF THE PUMP, RESPECTIVELY. WHEN THE PUMP OPERATES, A REACTION LIQUID IS DISCHARGED FROM THE DISCHARGED NOZZLE AND THEN SUCKED INTO THE SUCTION NOZZLE ALONG WITH CATALYST. THUS, CATALYST IS RECOVERED IN A CATALYST RECOVERY TANK PROVIDED BETWEEN THE SUCTION NOZZLE AND THE PUMP, AND THE REACTION LIQUID IS CIRCULATED FROM THE PUMP TO THE SUCTION NOZZLE THROUGH THE DISCHARGE NOZZLE. EITHER THE DISCHARGE NOZZLE OR THE SUCTION NOZZLE

    IS, AS OCCASION DEMANDS, SLID SO AS TO MAKE CONTACT WITH THE OTHER. THUS, THE INNER SURFACE OF THE SUCTION NOZZLE IS RINSED BY CIRCULATING A REACTION LIQUID, AND THEREBY CATALYST ADHERING TO THE INNER SURFACE OF THE SAID SUCTION NOZZLE IS REMOVED.

    Hci or hbr vapor carbonization of vegetable material in the manufacture of activated carbon
    144.
    发明授权
    Hci or hbr vapor carbonization of vegetable material in the manufacture of activated carbon 失效
    活性碳制品中的植物材料的HCI或HBR蒸气碳化

    公开(公告)号:US3557020A

    公开(公告)日:1971-01-19

    申请号:US69700868

    申请日:1968-01-11

    CPC classification number: C01B32/336

    Abstract: WOOD OR OTHER VEGETABLE MATERIAL HAVING A NON-UNIFORM SHAPE SUCH AS SHAPELESS PARTICLE POWDER, FLAKY POWDER, CHIP AND THE OTHERS IS CARBONIZED IN AN ACIDIC ATMOSPHERE CONTAINING VAPOR OR GAS OF HYDROCHLORIC OR HYDROBROMIC ACID OR ITS ANHYDRIDE FOR 10 MINUTES TO 10 HOURS AT A TEMPERATURE OF 80-1200* C. TO OBTAIN ACTIVATED CARBON OF SUPERIOR ADSORPTION ACTIVITY IN VERY HIGH YIELDS. IF DESIRED, THE ACTIVATED CARBON SO OBTAINED IS HEATED FURTHER IN AN ATMOSPHERE CONTAINING AN OXIDIZING GAS SUCH AS STEAM, CARBON DIOXIDE GAS OR AIR, OR IN AN INERT ATMOSPHERE TO IMPROVE THE ADSORPTION ACTIVITY OF SAID CARBON.

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