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    Recovering products from a by-products stream
    111.
    发明授权
    Recovering products from a by-products stream 失效
    从副产品流中恢复产品

    公开(公告)号：US5874651A

    公开(公告)日：1999-02-23

    申请号：US771545

    申请日：1996-12-23

    Applicant: Andrew J. McNabb ,  Rebecca E. Phillips

    Inventor： Andrew J. McNabb ,  Rebecca E. Phillips

    IPC: B01J3/00 ,  C07C27/02 ,  C07C29/80 ,  C07C29/88 ,  C07C31/20 ,  C07C45/85 ,  C07C27/26 ,  C07C35/08

    CPC classification number: C07C29/88 ,  B01J3/00 ,  C07C29/80 ,  C07C45/85

    Abstract: A process for increasing the amount of isolatable products in a by-product stream generated in the production of 1,6 hexanediol includes combining the by-product stream with water to form a combination of the water and the by-product stream; and reacting the combination at a temperature between about 250.degree. C. to about 400.degree. C. at a pressure from about 1,000 psig to about 3,000 psig to form one or more reaction products.

    Abstract translation: 在1,6,6-己二醇生产中产生的副产物流中增加可分离产物的量的方法包括将副产物流与水混合以形成水和副产物流的组合; 并在约250℃至约400℃的温度下在约1,000psig至约3,000psig的压力下使该组合反应以形成一种或多种反应产物。

    Pood freshener-warming device
    112.
    再颁专利
    Pood freshener-warming device 失效

    公开(公告)号：USRE28292E

    公开(公告)日：1975-01-07

    申请号：US26846172

    申请日：1972-07-03

    IPC: A21D17/00 ,  A47J27/04 ,  A47J39/02 ,  B01J3/00

    CPC classification number: A21D17/008 ,  A47J27/04 ,  B01J3/00

    Abstract: 1. A FOOD FRESHENER AND/OR WARMING DEVICE COMPRISING: A. CLOSED VESSEL; B. PARTITION MEANS WITHIN SAID VESSEL DIVIDING THE INTERIOR THEREOF INTO FIRST AND SECOND CHAMBERS; C. MEANS FOR CONTINUOUSLY (RECIRCULARING) CIRCULATING STEAM THROUGH SAID FIRST CHAMBER COMPRISING A STEAM INLET HAVING AN OPENING IN SAID FIRST CHAMBER SPACED ABOVE THE BOTTOM THEREOF AND A STEAM OUTLET HAVING AN OPENING DISPOSED IN THE BOTTOM OF SAID FIRST CHAMBER WHEREBY STEAM FROM A SOURCE THEREOF MAY BE CONTINUOUSLY CAUSED TO ENTER SAID FIRST CHAMBER THROUGH SAID STEAM INLET THEREOF, PASS THROUGH SAID FIRST CHAMBER AND EXIT SAID FIRST CHAMBER VIA SAID STEAM OUTLET THEREOF; D. PASSAGE MEANS HAVING AN INLET IN SAID FIRST CHAMBER AND AN OUTLET IN SAID SECOND CHAMBER; E. OPERATOR CONTROLLED VALVE MEANS FOR CONTROLLING THE FLOW OF STEAM THROUGH SAID PASSAGE MEANS FROM SAID FIRST CHAMBER TO SAID SECOND CHAMBER; AND F. APERTURE MEANS FOR APPLYING STEAM FROM SAID SECOND CHAMBER TO A FOOD ITEM.

    亜臨界水処理方法及び装置
    114.
    发明专利
    亜臨界水処理方法及び装置 有权
    亚临界水处理方法和装置

    公开(公告)号：JP2016022468A

    公开(公告)日：2016-02-08

    申请号：JP2014151244

    申请日：2014-07-24

    Applicant: 株式会社ピーシーエス

    Inventor： 鈴木 敏勝

    IPC: B09B3/00 ,  C02F11/08 ,  B01J3/02 ,  B01J3/04 ,  G21F9/30 ,  B01J3/00

    CPC classification number: B01J3/00 ,  B01J3/02 ,  B01J3/04 ,  B09B3/00 ,  C02F11/08 ,  G21F9/30

    Abstract: 【課題】有機系廃棄物や汚泥を、大型の圧力容器で少ないエネルギー消費量で分解する亜臨界水処理方法を提供する。 【解決手段】圧力容器内に高温、高圧の水蒸気を供給して、圧力容器内の有機系廃棄物や汚泥からなる処理対象物を攪拌しつつ加温、加圧し、圧力容器内の温度が150℃以上で、圧力容器内の温度及び圧力の少なくとも一方の急上昇を検出し、この検出の後、圧力容器内の温度を、急上昇開始時の温度以上に5〜10分間維持するように、水蒸気の供給量を調整し、その後、水蒸気の供給を停止する亜臨界水処理方法。 【選択図】図6

    Abstract translation: 要解决的问题：提供一种在大型压力容器中以少量能量分解有机废弃物和污泥的亚临界水处理方法。解决方案：在亚临界水处理方法中，通过供给压力容器来加热和加压 在压力容器中搅拌由有机废物和污泥组成的加工对象的高温高压蒸汽。 在压力容器中在检测到压力容器中的温度和压力中的至少一个温度和压力的急剧上升之后，调节蒸汽的供给量使得压力容器中的温度为 保持5-10分钟高于开始急升时的温度，然后停止供应蒸汽。选择图：图6

    Recovery method and apparatus noble gas
    115.
    发明专利
    Recovery method and apparatus noble gas 失效

    公开(公告)号：JP4112659B2

    公开(公告)日：2008-07-02

    申请号：JP33022897

    申请日：1997-12-01

    Applicant: 忠弘 大見 ,  大陽日酸株式会社

    Inventor： 忠弘 大見 ,  良夫 石原

    IPC: B01D53/46 ,  C01B23/00 ,  B01D53/00 ,  B01J3/00 ,  C23C16/44

    CPC classification number: C01B23/001 ,  B01D53/00 ,  B01D2256/18 ,  B01D2258/0216 ,  B01J3/00 ,  C23C16/4412

    Abstract: A process and an apparatus for recovering a noble gas, which can recover a noble gas exhausted from a noble gas employing system efficiently and also can supply the noble gas of a predetermined purity to the noble gas employing system and which can reduce consumption of the noble gas. In the process and apparatus for recovering a noble gas, when a noble gas contained in an exhaust gas exhausted from a noble gas employing system operated under reduced pressure is recovered, switching between introduction of the exhaust gas to a recovery system and exhaustion of the exhaust gas to an exhaust system is carried out under reduced pressure, and this switching operation is carried out depending on the content of impurity components contained in the exhaust gas or on the running state of the noble gas employing system.

    Variable pressure treatment of substance
    120.
    发明专利
    Variable pressure treatment of substance 失效
    可变压力处理物质

    公开(公告)号：JPS61141901A

    公开(公告)日：1986-06-28

    申请号：JP26453584

    申请日：1984-12-17

    Applicant: Mitsuo Sohgoh Kenkyusho Kk

    Inventor： MITSUO KOJI ,  OTSUBO NORIO ,  MITSUO MITSUKO ,  HIGAMI KYOKO

    IPC: B01D1/00 ,  B01D11/00 ,  B01D11/02 ,  B01D19/00 ,  B01J3/00

    CPC classification number: B01J3/00

    Abstract: PURPOSE:To perform sublimation, extraction, elution, evaporation and impregnation, by applying pressure change by atmospheric pressure to the solid or liquid in a hermetically sealed container. CONSTITUTION:A motor 16 is operated not only to rotate a stirring shaft 14 buy also to intermittently and continuously supply a material from a feeder 17. Valves 22, 11, 9, 19, 20 are closed while valves 5, 7 are opened and a vacuum sucking apparatus 2 is operated to evacuate a hermetically sealed container. At this time, evaporation and sublimation are performed. When the valves 11, 9 are opened, the open air is sucked to promote evaporation. Thereafter, the valve 20 is opened to return the container to atmospheric pressure and the valve 19 is opened to discharge the liquid in a gas-liquid separator 4 from a discharge pipe 18. This operation is repeated several times. If a treated substance remains, it is intermittently discharged from a discharge apparatus 3.

    Abstract translation: 目的：通过在气密密封的容器中对固体或液体施加大气压力的变化来进行升华，萃取，洗脱，蒸发和浸渍。 构成：马达16不仅使旋转搅拌轴14也可以间歇地连续地从进料器17供应材料。阀22,11,9和19,20关闭，同时阀5,7打开并且 操作真空吸入装置2以抽空密封容器。 此时，进行蒸发和升华。 当阀11,9打开时，抽吸露天气体以促进蒸发。 此后，打开阀门20使容器回到大气压力，打开阀门19，从排气管18排出气液分离器4中的液体。该操作重复多次。 如果处理物质残留，则从排放装置3间歇地排出。

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