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公开(公告)号:US07459072B2
公开(公告)日:2008-12-02
申请号:US10544427
申请日:2004-01-24
申请人: Stefan Bitterlich , Hartwig Voss , Gunter Schuch , Rudolf Sinnen , Heinrich Laib , Peter Paessler
发明人: Stefan Bitterlich , Hartwig Voss , Gunter Schuch , Rudolf Sinnen , Heinrich Laib , Peter Paessler
CPC分类号: B01D61/362 , C10G7/00 , C10G7/08 , C10G9/00 , C10G31/11
摘要: Process for the work-up of naphtha, wherein a) naphtha or a stream produced from naphtha in a pretreatment step is separated in a membrane unit into a stream A which is depleted in aromatics and a stream B which is enriched in aromatics, with the aromatics concentration in stream A being from 2 to 12% by weight (step a), b) at least part of the substream A is fed to a steam cracker (step b), c) at least part of the substream B is fed to a unit in which it is separated by means of a thermal process into a stream C which has a lower aromatics content than stream B or a plurality of streams C′, C″, C′″ . . . which each have lower aromatics contents than stream B and a stream D which has a higher aromatics content than stream B or a plurality of streams D′, D″, D′″ . . . which each have higher aromatics contents than stream B (step c), and d) the stream C or at least one of the streams C′, C″, C′″, in each case in part or in its entirety, is added to the feed to the steam cracker or fed into the steam cracker itself (step d).
摘要翻译: 用于处理石脑油的方法,其中a)在预处理步骤中将石脑油或由石脑油产生的物流在膜单元中分离成贫的芳烃流A和富含芳族化合物的物流B, 流A中的芳族化合物浓度为2至12重量%(步骤a),b)将至少部分分流A送入蒸汽裂解器(步骤b),c)将至少部分子流B送入 其中通过热处理将其分离成具有比流B或多个流C',C“,C”的较低芳烃含量的流C的单元。 。 。 其具有比流B更低的芳烃含量和具有比流B或多个流D',D“,D”'更高的芳族化合物含量的流D. 。 。 它们各自具有比物流B更高的芳烃含量(步骤c),以及d)在各种情况下部分或全部,流C或者流C',C“,C”'中的至少一个是 添加到蒸汽裂化器的进料中或者进入蒸汽裂化器本身(步骤d)。
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公开(公告)号:US5484941A
公开(公告)日:1996-01-16
申请号:US232291
申请日:1994-05-06
IPC分类号: C07D237/12 , C07D231/12
CPC分类号: C07D231/12
摘要: Process for the preparation of methylpyrazoles from diacetylene and hydrazines in which the diacetylene is removed from cracked gas by absorption and is then reacted with hydrazines.
摘要翻译: PCT No.PCT / EP92 / 02514 Sec。 371日期:1994年5月6日 102(e)日期1994年5月6日PCT提交1992年11月3日PCT公布。 WO93 / 10098 PCT出版物 日期:1993年5月27日。从乙炔和肼制备甲基吡唑的方法,其中通过吸收将二乙炔从裂化气体中除去,然后与肼反应。
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公开(公告)号:US06984317B2
公开(公告)日:2006-01-10
申请号:US10762433
申请日:2004-01-22
申请人: William C. Hiatt , James R. Brocato , Olaf McDavid , Murthy S. Duvvuri , Donald O. Lierman , Uwe Wegmann , Peter Paessler
发明人: William C. Hiatt , James R. Brocato , Olaf McDavid , Murthy S. Duvvuri , Donald O. Lierman , Uwe Wegmann , Peter Paessler
IPC分类号: C02F3/00
CPC分类号: C02F3/12 , C02F1/54 , C02F3/006 , C02F3/302 , C02F2209/04 , C02F2209/06 , C02F2209/22 , Y02W10/15
摘要: A system and method for treatment of soot-laden waste water is disclosed. The method comprises the steps of separating the soot from the waste water initially in a clarifier. The concentrated soot is then treated with an activated sludge mixture in a digester with a very long average hydraulic retention time to effectively digest the materials found in the concentrated soot. Soot-free waste water is treated via standard aerobic, and anoxic reactor basins and a clarifier with activated sludge recirculation. The system effectively removes soot from soot-laden waste water in a cost effective manner.
摘要翻译: 公开了一种用于处理含烟灰的废水的系统和方法。 该方法包括以下步骤:最初在澄清池中从废水中分离烟灰。 然后将浓缩烟灰用消化器中的活性污泥混合物处理,其具有非常长的平均水力停留时间,以有效消化浓缩烟灰中发现的物质。 无烟废水通过标准有氧和缺氧反应器池和带有活性污泥再循环的澄清池进行处理。 该系统以成本有效的方式有效地从含烟灰的废水中去除烟灰。
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公开(公告)号:US06733672B2
公开(公告)日:2004-05-11
申请号:US10039829
申请日:2001-10-19
申请人: William C. Hiatt , James R. Brocato , Olaf McDavid , Murthy S. Duvvuri , Donald O. Lierman , Uwe Wegmann , Peter Paessler
发明人: William C. Hiatt , James R. Brocato , Olaf McDavid , Murthy S. Duvvuri , Donald O. Lierman , Uwe Wegmann , Peter Paessler
IPC分类号: C02F300
CPC分类号: C02F3/12 , C02F1/54 , C02F3/006 , C02F3/302 , C02F2209/04 , C02F2209/06 , C02F2209/22 , Y02W10/15
摘要: A system and method for treatment of soot-laden waste water is disclosed. The method comprises the steps of separating the soot from the waste water initially in a clarifier. The concentrated soot is then treated with an activated sludge mixture in a digester with a very long average hydraulic retention time to effectively digest the materials found in the concentrated soot. Soot-free waste water is treated via standard aerobic, and anoxic reactor basins and a clarifier with activated sludge recirculation. The system effectively removes soot from soot-laden waste water in a cost effective manner.
摘要翻译: 公开了一种用于处理含烟灰的废水的系统和方法。 该方法包括以下步骤:最初在澄清池中从废水中分离烟灰。 然后将浓缩烟灰用消化器中的活性污泥混合物处理,其具有非常长的平均水力停留时间,以有效消化浓缩烟灰中发现的物质。 无烟废水通过标准有氧和缺氧反应器池和带有活性污泥再循环的澄清池进行处理。 该系统以成本有效的方式有效地从含烟灰的废水中去除烟灰。
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