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公开(公告)号：US5520818A
公开(公告)日：1996-05-28
申请号：US313153
申请日：1994-11-29
IPC分类号： A62D3/00 , B01D21/00 , B01D53/18 , B01D53/52 , B01D53/74 , B01D53/78 , B01F3/04 , B01F7/00 , B03D1/02 , B03D1/16 , C01B17/02 , C01B17/05 , C01F11/18 , C02F1/20 , C02F1/72 , C02F1/76 , C02F1/78 , C02F3/20 , C01B17/16 , B01D21/26
CPC分类号： C02F3/205 , B01D21/0042 , B01D21/2427 , B01D21/2438 , B01D21/2494 , B01D21/26 , B01D53/18 , B01D53/52 , B01D53/74 , B01D53/78 , B01F3/04539 , B01F3/04609 , B01F3/04617 , B01F3/04836 , B03D1/02 , B03D1/04 , B03D1/1493 , B03D1/16 , C01B17/0232 , C01B17/05 , C01F11/181 , C02F1/20 , C02F1/72 , C02F1/76 , B01D2221/04 , B01D2251/90 , B01D2251/902 , B01F7/00291 , B03D1/1462 , C02F1/725 , C02F1/78 , Y02W10/15
摘要： Components, usually but not exclusively gaseous components, are removed in a liquid medium from gas streams and chemically converted into an insoluble phase or physically removed. Specifically, hydrogen sulfide may be removed from gas streams by oxidation in aqueous chelated transition metal solution in a modified agitated flotation cell. The same principal may be employed in other procedures in which a gaseous phase is dispersed in a liquid phase to effect an interaction between components present in such phases. A gas-liquid contact apparatus, generally a combined chemical reactor and solid product separation device, comprising such modified agitated flotation cell is also described. In order to effect mass transfer and rapid reaction gas bubbles containing hydrogen sulfide and oxygen are formed by rotating an impeller at a blade tip velocity of at least about 350 in/sec. to achieve the required shear. To assist in the reaction, a surrounding shroud has a plurality of openings, generally of aspect ratio of approximately 1, of equal diameter and arranged in uniform pattern, such as to provide a gas flow therethrough less than about 0.02 lb/min/opening in the shroud. In general, the gas velocity index of gas through the openings in the shroud is at least about 18 per second per opening. Each of the openings has an area corresponding to an equivalent diameter of less than about one inch.
摘要翻译： PCT No.PCT / CA93 / 00148 Sec。 371日期：1994年11月29日 102（e）日期1994年11月29日PCT 1993年4月5日PCT公布。 出版物WO93 / 19836 日期：1993年10月14日。通常但不排除气体组分的组分在液体介质中从气流中除去并化学转化成不溶相或物理去除。 具体地，硫化氢可以通过在改性的搅拌浮选槽中的水性螯合过渡金属溶液中的氧化从气流中除去。 在其中气相分散在液相中以实现在这些相中存在的组分之间的相互作用的其它方法中可使用相同的原子。 还描述了气液接触装置，通常是组合的化学反应器和固体产物分离装置，其包括这种改性的搅拌浮选槽。 为了进行质量传递和快速反应，通过以至少约350in / sec的叶片尖端速度旋转叶轮来形成含有硫化氢和氧气的气泡。 达到要求的剪切。 为了帮助反应，周围的护罩具有多个开口，通常具有相当直径的纵横比约为1的开口，并以均匀的图案排列，例如提供通过其中的小于约0.02磅/分钟/开口的气流 护罩。 通常，通过护罩中的开口的气体的气体速度指数为每个开口每秒至少约18个。 每个开口具有对应于小于约一英寸的等效直径的面积。
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2.发明授权
公开(公告)号：US5527475A
公开(公告)日：1996-06-18
申请号：US465227
申请日：1995-06-05
IPC分类号： A62D3/00 , B01D21/00 , B01D53/18 , B01D53/52 , B01D53/74 , B01D53/78 , B01F3/04 , B01F7/00 , B03D1/02 , B03D1/16 , C01B17/02 , C01B17/05 , C01F11/18 , C02F1/20 , C02F1/72 , C02F1/76 , C02F1/78 , C02F3/20 , B01D21/26 , B03D1/00
CPC分类号： C02F3/205 , B01D21/0042 , B01D21/2427 , B01D21/2438 , B01D21/2494 , B01D21/26 , B01D53/18 , B01D53/52 , B01D53/74 , B01D53/78 , B01F3/04539 , B01F3/04609 , B01F3/04617 , B01F3/04836 , B03D1/02 , B03D1/04 , B03D1/1493 , B03D1/16 , C01B17/0232 , C01B17/05 , C01F11/181 , C02F1/20 , C02F1/72 , C02F1/76 , B01D2221/04 , B01D2251/90 , B01D2251/902 , B01F7/00291 , B03D1/1462 , C02F1/725 , C02F1/78 , Y02W10/15
摘要： The parameters of a gas-liquid contact apparatus for the removal of a component of a gas stream in which an impeller-apertured shroud combination is immersed in a liquid phase to which the gas stream is fed at a gas flow rate of Q. The structural and operating parameters of the apparatus are quantified to provide a Shear Effectiveness Index (SEI) value of from about 1 to about 10 and an Effective Shear Index (ESI) value of from about 1 to about 2500.
摘要翻译： 用于去除气流的组分的气液接触装置的参数，其中叶轮孔径的罩组合浸入气体以气体流量Q供给的液相中。结构 并对装置的操作参数进行定量，以提供约1至约10的剪切效应指数（SEI）值和约1至约2500的有效剪切指数（ESI）值。
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公开(公告)号：US5585005A
公开(公告)日：1996-12-17
申请号：US462161
申请日：1995-06-05
IPC分类号： A62D3/00 , B01D21/00 , B01D53/18 , B01D53/52 , B01D53/74 , B01D53/78 , B01F3/04 , B01F7/00 , B03D1/02 , B03D1/16 , C01B17/02 , C01B17/05 , C01F11/18 , C02F1/20 , C02F1/72 , C02F1/76 , C02F1/78 , C02F3/20
CPC分类号： C02F3/205 , B01D21/0042 , B01D21/2427 , B01D21/2438 , B01D21/2494 , B01D21/26 , B01D53/18 , B01D53/52 , B01D53/74 , B01D53/78 , B01F3/04539 , B01F3/04609 , B01F3/04617 , B01F3/04836 , B03D1/02 , B03D1/04 , B03D1/1493 , B03D1/16 , C01B17/0232 , C01B17/05 , C01F11/181 , C02F1/20 , C02F1/72 , C02F1/76 , B01D2221/04 , B01D2251/90 , B01D2251/902 , B01F7/00291 , B03D1/1462 , C02F1/725 , C02F1/78 , Y02W10/15
摘要： Components, usually but not exclusively gaseous components, are removed in a liquid medium from gas streams and chemically converted into an insoluble phase or physically removed. Specifically, hydrogen sulfide may be removed from gas streams by oxidation in aqueous chelated transition metal solution in a agitated flotation cell. The same principal may be employed with other procedures in which a gaseous phase is dispersed in a liquid phase to effect an interaction between components present in such phases, for example, to treat or strip or react a component of the liquid phase.
摘要翻译： 组分通常但不排他气体组分在液体介质中从气流中除去并化学转化为不溶相或物理去除。 具体地，硫化氢可以通过在搅拌浮选槽中的水性螯合过渡金属溶液中的氧化从气流中除去。 可以使用相同的原理与其中气相分散在液相中以实现在这些相中存在的组分之间的相互作用的其它方法，例如处理或剥离或反应液相的组分。
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公开(公告)号：US5352421A
公开(公告)日：1994-10-04
申请号：US863720
申请日：1992-04-03
IPC分类号： A62D3/00 , A62D3/38 , A62D101/20 , A62D101/47 , B01D21/00 , B01D53/18 , B01D53/52 , B01D53/74 , B01D53/78 , B01F3/04 , B01F7/00 , B01J10/00 , B03D1/02 , B03D1/16 , C01B17/05 , C02F1/24 , C02F1/72 , C02F1/78 , C02F3/20 , C01B17/16 , B05B7/10 , C01B17/20 , C01B31/20
CPC分类号： A62D3/38 , B01D21/2427 , B01D21/2433 , B01D21/2494 , B01D21/26 , B01D53/18 , B01D53/52 , B01D53/74 , B01D53/78 , B01F3/04539 , B01F3/04609 , B01F3/04617 , B01F3/04836 , B03D1/02 , B03D1/1462 , B03D1/16 , C01B17/05 , C02F3/205 , A62D2101/20 , A62D2101/47 , A62D2203/10 , B01F2003/04553 , B01F2003/0468 , B01F7/00291 , C02F1/725 , C02F1/78 , Y02W10/15
摘要： Components, usually but not exclusively gaseous components, are removed in a liquid medium from gas streams and chemically converted into an insoluble phase or physically removed. Specifically, hydrogen sulfide may be removed from gas streams by oxidation in aqueous chelated transition metal solution in a modified agitated flotation cell. The same principle may be employed with other procedures in which a gaseous phase is dispersed in a liquid phase to effect an interaction between components present in such phases. A gas-liquid contact apparatus, generally a combined chemical reactor and solid product separation device, comprising such modified agitated flotation cell also is described. In order to effect efficient mass transfer and rapid reaction, gas bubbles containing hydrogen sulfide and oxygen are formed by rotating an impeller at a blade tip velocity of at least about 350 in/sec. to achieve the required shear. To assist in the reaction, a surrounding shroud has a plurality of openings, generally of aspect ratio of approximately 1, of equal diameter and arranged in uniform pattern, such as to provide a gas flow therethrough less than about 0.02 lb/min/opening in the shroud. In general, the gas velocity index of gas through the openings in the shroud is at least about 18 per second per opening, preferably at least about 24 per second per opening. Each of the openings has an area corresponding to an equivalent diameter less than about one inch.
摘要翻译： 组分通常但不排他气体组分在液体介质中从气流中除去并化学转化为不溶相或物理去除。 具体地，硫化氢可以通过在改性的搅拌浮选槽中的水性螯合过渡金属溶液中的氧化从气流中除去。 相同的原理可以用于其中气相分散在液相中以实现在这些相中存在的组分之间的相互作用的其它方法。 还描述了包括这种改进的搅拌浮选槽的气液接触装置，通常是组合的化学反应器和固体产物分离装置。 为了实现有效的传质和快速反应，通过以至少约350in / sec的叶片尖速度旋转叶轮来形成含有硫化氢和氧气的气泡。 达到要求的剪切。 为了帮助反应，周围的护罩具有多个开口，通常具有相当直径的纵横比约为1的开口，并以均匀的图案排列，例如提供通过其中的小于约0.02磅/分钟/开口的气流 护罩。 通常，通过护罩中的开口的气体的气体速度指数为每个开口每秒至少约18次，优选每个开口每秒至少约24次。 每个开口具有对应于小于约一英寸的当量直径的面积。
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公开(公告)号：US5500130A
公开(公告)日：1996-03-19
申请号：US462166
申请日：1995-06-05
IPC分类号： B01D21/00 , B01D21/26 , B01D53/18 , B01D53/52 , B01D53/78 , C01B17/02 , C01B17/05 , C01F11/18 , C02F1/20 , C02F1/72 , C02F1/76 , C02F1/78 , C01B17/16
CPC分类号： B03D1/16 , B01D21/0042 , B01D21/2427 , B01D21/2438 , B01D21/2494 , B01D21/26 , B01D53/18 , B01D53/52 , B01D53/78 , B03D1/04 , B03D1/1493 , C01B17/0232 , C01B17/05 , C01F11/181 , C02F1/20 , C02F1/72 , C02F1/76 , B01D2221/04 , B01D2251/90 , B01D2251/902 , B03D1/1462 , C02F1/78
摘要： Components, usually but not exclusively gaseous components, are removed in a liquid medium from gas streams and chemically converted into an insoluble phase or physically removed. Specifically, hydrogen sulfide may be removed from gas streams by oxidation in aqueous chelated transition metal solution in a modified agitated flotation cell. The same principal may be employed in other procedures in which a gaseous phase is dispersed in a liquid phase to effect an interaction between components present in such phases. A gas-liquid contact apparatus, generally a combined chemical reactor and solid product separation device, comprising such modified agitated flotation cell is also described. In order to effect mass transfer and rapid reaction gas bubbles containing hydrogen sulfide and oxygen are formed by rotating an impeller at a blade tip velocity of at least about 350 in/sec. to achieve the required shear. To assist in the reaction, a surrounding shroud has a plurality of openings, generally of aspect ratio of approximately 1, of equal diameter and arranged in uniform pattern, such as to provide a gas flow therethrough less than about 0.02 lb/min/opening in the shroud. In general, the gas velocity index of gas through the openings in the shroud is at least about 18 per second per opening. Each of the openings has an area corresponding to an equivalent diameter of less than about one inch.
摘要翻译： 组分通常但不排他气体组分在液体介质中从气流中除去并化学转化为不溶相或物理去除。 具体地，硫化氢可以通过在改性的搅拌浮选槽中的水性螯合过渡金属溶液中的氧化从气流中除去。 在其中气相分散在液相中以实现在这些相中存在的组分之间的相互作用的其它方法中可使用相同的原子。 还描述了气液接触装置，通常是组合的化学反应器和固体产物分离装置，其包括这种改性的搅拌浮选槽。 为了进行质量传递和快速反应，通过以至少约350in / sec的叶片尖端速度旋转叶轮来形成含有硫化氢和氧气的气泡。 达到要求的剪切。 为了帮助反应，周围的护罩具有多个开口，通常具有相当直径的纵横比约为1的开口，并以均匀的图案排列，例如提供通过其中的小于约0.02磅/分钟/开口的气流 护罩。 通常，通过护罩中的开口的气体的气体速度指数为每个开口每秒至少约18个。 每个开口具有对应于小于约一英寸的等效直径的面积。
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公开(公告)号：US5366698A
公开(公告)日：1994-11-22
申请号：US863692
申请日：1992-05-20
IPC分类号： A62D3/00 , B01D21/00 , B01D53/18 , B01D53/52 , B01D53/74 , B01D53/78 , B01F3/04 , B01F7/00 , B03D1/02 , B03D1/16 , C01B17/05 , C02F1/72 , C02F1/78 , C02F3/20 , B01D53/34 , B01F5/12 , B01F13/02 , F01N3/00
CPC分类号： C02F3/205 , B01D21/2438 , B01D21/2494 , B01D53/18 , B01D53/52 , B01D53/74 , B01D53/78 , B01F3/04539 , B01F3/04609 , B01F3/04617 , B01F3/04836 , B03D1/02 , B03D1/04 , B03D1/1493 , B03D1/16 , C01B17/05 , B01F7/00291 , B03D1/1462 , C02F1/725 , C02F1/78 , Y02W10/15
摘要： Components, usually but not exclusively gaseous components, are removed in a liquid medium from gas streams and chemically converted into an insoluble phase or physically removed. Specifically, hydrogen sulfide may be removed from gas streams by oxidation in aqueous chelated transition metal solution in a modified agitated flotation cell. A gas-liquid contact apparatus, generally a combined chemical reactor and solid product separation device, comprising such modified agitated flotation cell also is described. In order to effect efficient mass transfer and rapid reaction, gas bubbles containing hydrogen sulfide and oxygen are formed by rotating an impeller at a blade tip velocity of at least about 350 in/sec. to achieve the required shear. To assist in the reaction, a surrounding shroud has a plurality of openings, generally of aspect ratio of approximately 1, of equal diameter and arranged in uniform pattern, such as to provide a gas flow therethrough less than about 0.02 lb/min/opening in the shroud. In general, the gas velocity index is at least about 18 per second per opening, preferably at least about 24 per second per opening. Each of the openings has an area corresponding to an equivalent diameter less than about one inch.
摘要翻译： 组分通常但不排他气体组分在液体介质中从气流中除去并化学转化为不溶相或物理去除。 具体地，硫化氢可以通过在改性的搅拌浮选槽中的水性螯合过渡金属溶液中的氧化从气流中除去。 还描述了包括这种改进的搅拌浮选槽的气液接触装置，通常是组合的化学反应器和固体产物分离装置。 为了实现有效的传质和快速反应，通过以至少约350in / sec的叶片尖速度旋转叶轮来形成含有硫化氢和氧气的气泡。 达到要求的剪切。 为了帮助反应，周围的护罩具有多个开口，通常具有相当直径的纵横比约为1的开口，并以均匀的图案排列，例如提供通过其中的小于约0.02磅/分钟/开口的气流 护罩。 通常，气体速度指数为每个开口至少约18秒，优选每个开口至少约24秒。 每个开口具有对应于小于约一英寸的当量直径的面积。
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公开(公告)号：US5174973A
公开(公告)日：1992-12-29
申请号：US622485
申请日：1990-12-05
IPC分类号： A62D3/00 , B01D53/18 , B01D53/52 , B01D53/78 , B01F3/04 , B01F7/00 , B03D1/02 , B03D1/16 , C01B17/05
CPC分类号： C01B17/05 , B01D53/18 , B01D53/52 , B01D53/78 , B01F3/04609 , B01F3/04617 , B03D1/02 , B03D1/04 , B03D1/1493 , B03D1/16 , B01F7/00291 , B03D1/1462
摘要： Components, usually but not exclusively gaseous components, are removed in a liquid medium from gas streams and chemically converted into an insoluble phase or physically removed. Specifically, hydrogen sulfide may be removed from streams by oxidation in aqueous chelated transition metal solution in a modified agitated flotation cell. A gas-liquid contact apparatus, generally a combined chemical reactor and solid product separation device, comprising such modified agitated flotation cell also is described. In order to effect efficient mass transfer and rapid reaction, gas bubbles containing hydrogen sulfide and oxygen are formed by rotating an impeller at a blade tip velocity of at least about 350 in/sec. to achieve the required shear. To assist in the reaction, a surrounding shroud has a plurality of openings, generally of aspect ratio of approximately 1, of equal diameter and arranged in uniform pattern, such as to provide a gas flow therethrough less than about 0.02 lb/min/opening in the shroud. In general, the gas velocity index is at least about 18 per second per opening, preferably at least about 24 per second per opening. Each of the openings has an area corresponding to an equivalent diameter less than about one inch.
摘要翻译： 组分通常但不排他气体组分在液体介质中从气流中除去并化学转化为不溶相或物理去除。 具体地，硫化氢可以通过在改性搅拌浮选槽中的螯合过渡金属溶液中的氧化而从流中除去。 还描述了包括这种改进的搅拌浮选槽的气液接触装置，通常是组合的化学反应器和固体产物分离装置。 为了实现有效的传质和快速反应，通过以至少约350in / sec的叶片尖速度旋转叶轮来形成含有硫化氢和氧气的气泡。 达到要求的剪切。 为了帮助反应，周围的护罩具有多个开口，通常具有相当直径的纵横比约为1的开口，并以均匀的图案排列，例如提供通过其中的小于约0.02磅/分钟/开口的气流 护罩。 通常，气体速度指数为每个开口至少约18秒，优选每个开口至少约24秒。 每个开口具有对应于小于约一英寸的当量直径的面积。
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公开(公告)号：US5552061A
公开(公告)日：1996-09-03
申请号：US463965
申请日：1995-06-05
IPC分类号： A62D3/00 , B01D21/00 , B01D53/18 , B01D53/52 , B01D53/74 , B01D53/78 , B01F3/04 , B01F7/00 , B03D1/02 , B03D1/16 , C01B17/02 , C01B17/05 , C01F11/18 , C02F1/20 , C02F1/72 , C02F1/76 , C02F1/78 , C02F3/20 , C01B17/16 , B05B7/10
CPC分类号： C02F3/205 , B01D21/0042 , B01D21/2427 , B01D21/2438 , B01D21/2494 , B01D21/26 , B01D53/18 , B01D53/52 , B01D53/74 , B01D53/78 , B01F3/04539 , B01F3/04609 , B01F3/04617 , B01F3/04836 , B03D1/02 , B03D1/04 , B03D1/1493 , B03D1/16 , C01B17/0232 , C01B17/05 , C01F11/181 , C02F1/20 , C02F1/72 , C02F1/76 , B01D2221/04 , B01D2251/90 , B01D2251/902 , B01F7/00291 , B03D1/1462 , C02F1/725 , C02F1/78 , Y02W10/15
摘要： Viscous liquids, such as liquid sulfur and bitumen asphalt are contacted with gases to strip absorbed gases from the viscous liquid and/or transfer gaseous components into the viscous liquid using a shrouded impeller combination immersed in the viscous liquid. The invention has particular application to the stripping of hydrogen sulfide and hydrogen polysulfides from liquid sulfur using an oxidizing gas.
摘要翻译： 粘性液体，例如液体硫和沥青沥青与气体接触以从粘性液体中除去吸收的气体和/或使用浸入粘性液体中的带有罩的叶轮组合物将气体组分转移到粘性液体中。 本发明特别适用于使用氧化气体从液态硫中汽提硫化氢和多硫化氢。
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公开(公告)号：US5500135A
公开(公告)日：1996-03-19
申请号：US462157
申请日：1995-06-05
IPC分类号： A62D3/00 , B01D21/00 , B01D53/18 , B01D53/52 , B01D53/74 , B01D53/78 , B01F3/04 , B01F7/00 , B03D1/02 , B03D1/16 , C01B17/02 , C01B17/05 , C01F11/18 , C02F1/20 , C02F1/72 , C02F1/76 , C02F1/78 , C02F3/20 , C01B17/16 , B01D21/26
CPC分类号： C02F3/205 , B01D21/0042 , B01D21/2427 , B01D21/2438 , B01D21/2494 , B01D21/26 , B01D53/18 , B01D53/52 , B01D53/74 , B01D53/78 , B01F3/04539 , B01F3/04609 , B01F3/04617 , B01F3/04836 , B03D1/02 , B03D1/04 , B03D1/1493 , B03D1/16 , C01B17/0232 , C01B17/05 , C01F11/181 , C02F1/20 , C02F1/72 , C02F1/76 , B01D2221/04 , B01D2251/90 , B01D2251/902 , B01F7/00291 , B03D1/1462 , C02F1/725 , C02F1/78 , Y02W10/15
摘要： Components, usually but not exclusively gaseous components, are removed in a liquid medium from gas streams and chemically converted into an insoluble phase or physically removed. Specifically, hydrogen sulfide may be removed from gas streams by oxidation in aqueous chelated transition metal solution in a modified agitated flotation cell. The same principal may be employed in other procedures in which a gaseous phase is dispersed in a liquid phase to effect an interaction between components present in such phases. A gas-liquid contact apparatus, generally a combined chemical reactor and solid product separation device, comprising such modified agitated flotation cell is also described. In order to effect mass transfer and rapid reaction gas bubbles containing hydrogen sulfide and oxygen are formed by rotating an impeller at a blade tip velocity of at least about 350 in/sec. to achieve the required shear. To assist in the reaction, a surrounding shroud has a plurality of openings, generally of aspect ratio of approximately 1, of equal diameter and arranged in uniform pattern, such as to provide a gas flow therethrough less than about 0.02 lb/min/opening in the shroud. In general, the gas velocity index of gas through the openings in the shroud is at least about 18 per second per opening. Each of the openings has an area corresponding to an equivalent diameter of less than about one inch.
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公开(公告)号：US5413765A
公开(公告)日：1995-05-09
申请号：US230230
申请日：1994-04-20
IPC分类号： A62D3/00 , A62D3/38 , A62D101/20 , A62D101/47 , B01D21/00 , B01D53/18 , B01D53/52 , B01D53/74 , B01D53/78 , B01F3/04 , B01F7/00 , B01J10/00 , B03D1/02 , B03D1/16 , C01B17/05 , C02F1/24 , C02F1/72 , C02F1/78 , C02F3/20 , B01F5/06 , B01F13/02
CPC分类号： A62D3/38 , B01D21/2427 , B01D21/2433 , B01D21/2494 , B01D21/26 , B01D53/18 , B01D53/52 , B01D53/74 , B01D53/78 , B01F3/04539 , B01F3/04609 , B01F3/04617 , B01F3/04836 , B03D1/02 , B03D1/1462 , B03D1/16 , C01B17/05 , C02F3/205 , A62D2101/20 , A62D2101/47 , A62D2203/10 , B01F2003/04553 , B01F2003/0468 , B01F7/00291 , C02F1/725 , C02F1/78 , Y02W10/15
摘要： Components, usually but not exclusively gaseous components, are removed in a liquid medium from gas streams and chemically converted into an insoluble phase or physically removed. Specifically, hydrogen sulfide may be removed from gas streams by oxidation in aqueous chelated transition metal solution in a modified agitated flotation cell. The same principle may be employed with other procedures in which a gaseous phase is dispersed in a liquid phase to effect an interaction between components present in such phases. A gas-liquid contact apparatus, generally a combined chemical reactor and solid product separation device, comprising such modified agitated flotation cell also is described. In order to effect efficient mass transfer and rapid reaction, gas bubbles containing hydrogen sulfide and oxygen are formed by rotating an impeller at a blade tip velocity of at least about 350 in/sec. to achieve the required shear. To assist in the reaction, a surrounding shroud has a plurality of openings, generally of aspect ratio of approximately 1, of equal diameter and arranged in uniform pattern, such as to provide a gas flow therethrough less than about 0.02 lb/min/opening in the shroud. In general, the gas velocity index of gas through the openings in the shroud is at least about 18 per second per opening, preferably at least about 24 per second per opening. Each of the openings has an area corresponding to an equivalent diameter less than about one inch.
摘要翻译： 组分通常但不排他气体组分在液体介质中从气流中除去并化学转化为不溶相或物理去除。 具体地，硫化氢可以通过在改性的搅拌浮选槽中的水性螯合过渡金属溶液中的氧化从气流中除去。 相同的原理可以用于其中气相分散在液相中以实现在这些相中存在的组分之间的相互作用的其它方法。 还描述了包括这种改进的搅拌浮选槽的气液接触装置，通常是组合的化学反应器和固体产物分离装置。 为了实现有效的传质和快速反应，通过以至少约350in / sec的叶片尖速度旋转叶轮来形成含有硫化氢和氧气的气泡。 达到要求的剪切。 为了帮助反应，周围的护罩具有多个开口，通常具有相当直径的纵横比约为1的开口，并以均匀的图案排列，例如提供通过其中的小于约0.02磅/分钟/开口的气流 护罩。 通常，通过护罩中的开口的气体的气体速度指数为每个开口每秒至少约18次，优选每个开口每秒至少约24次。 每个开口具有对应于小于约一英寸的当量直径的面积。
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