Butadiene extraction process
    3.
    发明授权

    公开(公告)号:US09744475B2

    公开(公告)日:2017-08-29

    申请号:US15059771

    申请日:2016-03-03

    CPC classification number: B01D3/40 B01D3/143 B01D19/0068 C07C7/08 C07C11/167

    Abstract: A process for recovering 1,3-butadiene from a C4 fraction, where the butadiene extraction processes may be operated at an intermediate pressure using a liquid ring type compressor. The use of a liquid ring compressor, among other process options presented herein, may advantageously reduce capital and operating costs, similar to the compressorless option, while mitigating the risks associated with the higher operating temperatures and pressures associated with the compressorless option. Thus, the embodiments of the processes disclosed herein encompass the best features of the conventional design (low pressure, with a compressor) with the advantages of the compressorless design (low capital and operating cost), as well as other advantages unique to the systems disclosed herein.

    Butadiene extraction process
    4.
    发明授权
    Butadiene extraction process 有权
    丁二烯提取工艺

    公开(公告)号:US09296667B2

    公开(公告)日:2016-03-29

    申请号:US14058637

    申请日:2013-10-21

    CPC classification number: B01D3/40 B01D3/143 B01D19/0068 C07C7/08 C07C11/167

    Abstract: A process for recovering 1,3-butadiene from a C4 fraction, where the butadiene extraction processes may be operated at an intermediate pressure using a liquid ring type compressor. The use of a liquid ring compressor, among other process options presented herein, may advantageously reduce capital and operating costs, similar to the compressorless option, while mitigating the risks associated with the higher operating temperatures and pressures associated with the compressorless option. Thus, the embodiments of the processes disclosed herein encompass the best features of the conventional design (low pressure, with a compressor) with the advantages of the compressorless design (low capital and operating cost), as well as other advantages unique to the systems disclosed herein.

    Abstract translation: 从C4级分回收1,3-丁二烯的方法,其中丁二烯萃取方法可以使用液环式压缩机在中间压力下操作。 使用液环式压缩机以及本文提供的其它过程选项可有利地减少与无压缩机选项类似的资本和操作成本,同时减轻与无压缩机选择相关联的较高操作温度和压力相关的风险。 因此,本文公开的方法的实施例包括具有无压缩机设计(低资本和运行成本)的优点的传统设计(具有压缩机的低压力)的最佳特征以及公开的系统独有的其它优点 这里。

    Selective olefin extraction
    5.
    发明授权

    公开(公告)号:US09776103B2

    公开(公告)日:2017-10-03

    申请号:US15196297

    申请日:2016-06-29

    Abstract: A process and system for separating butenes and butanes by extractive distillation using a polar solvent is disclosed. The process may include: contacting a hydrocarbon mixture including butanes and butenes with a lean solvent mixture in an extractive distillation column to form an enriched solvent fraction comprising butenes; recovering an overheads fraction comprising butanes and a bottoms fraction from the extractive distillation column; feeding the bottoms fraction to a stripper including a stripping section and a wash section; recovering the lean solvent mixture as a bottoms fraction and a stripper overheads fraction comprising butenes and water from the stripper; condensing the overheads fraction to form a water fraction and a product butenes fraction; feeding water as reflux to a top of the stripper wash section; feeding at least a portion of the condensed water fraction intermediate the top and bottom of the stripper wash section as a second reflux.

    SELECTIVE OLEFIN EXTRACTION
    7.
    发明申请
    SELECTIVE OLEFIN EXTRACTION 审中-公开
    选择性烯醇提取

    公开(公告)号:US20160303489A1

    公开(公告)日:2016-10-20

    申请号:US15196297

    申请日:2016-06-29

    Abstract: A process and system for separating butenes and butanes by extractive distillation using a polar solvent is disclosed. The process may include: contacting a hydrocarbon mixture including butanes and butenes with a lean solvent mixture in an extractive distillation column to form an enriched solvent fraction comprising butenes; recovering an overheads fraction comprising butanes and a bottoms fraction from the extractive distillation column; feeding the bottoms fraction to a stripper including a stripping section and a wash section; recovering the lean solvent mixture as a bottoms fraction and a stripper overheads fraction comprising butenes and water from the stripper; condensing the overheads fraction to form a water fraction and a product butenes fraction; feeding water as reflux to a top of the stripper wash section; feeding at least a portion of the condensed water fraction intermediate the top and bottom of the stripper wash section as a second reflux.

    Abstract translation: 公开了一种使用极性溶剂通过萃取蒸馏分离丁烯和丁烷的方法和系统。 该方法可以包括:将包含丁烷和丁烯的烃混合物与萃取蒸馏塔中的贫溶剂混合物接触以形成包含丁烯的富集溶剂馏分; 从萃取蒸馏塔回收包含丁烷和塔底馏分的塔顶馏分; 将塔底馏分进料到包括汽提段和洗涤段的汽提塔中; 回收作为底部馏分的贫溶剂混合物和从汽提器中除去含有丁烯和水的汽提塔顶馏分; 冷凝塔顶馏分以形成水分和产物丁烯级分; 将水作为回流进料至脱胶器洗涤部分的顶部; 将至少一部分冷凝水部分作为第二回流供入汽提器洗涤部分的顶部和底部。

    BUTADIENE EXTRACTION PROCESS
    8.
    发明申请
    BUTADIENE EXTRACTION PROCESS 审中-公开
    二倍体提取过程

    公开(公告)号:US20160184732A1

    公开(公告)日:2016-06-30

    申请号:US15059771

    申请日:2016-03-03

    CPC classification number: B01D3/40 B01D3/143 B01D19/0068 C07C7/08 C07C11/167

    Abstract: A process for recovering 1,3-butadiene from a C4 fraction, where the butadiene extraction processes may be operated at an intermediate pressure using a liquid ring type compressor. The use of a liquid ring compressor, among other process options presented herein, may advantageously reduce capital and operating costs, similar to the compressorless option, while mitigating the risks associated with the higher operating temperatures and pressures associated with the compressorless option. Thus, the embodiments of the processes disclosed herein encompass the best features of the conventional design (low pressure, with a compressor) with the advantages of the compressorless design (low capital and operating cost), as well as other advantages unique to the systems disclosed herein.

    Abstract translation: 从C4级分回收1,3-丁二烯的方法,其中丁二烯萃取方法可以使用液环式压缩机在中间压力下操作。 使用液环式压缩机以及本文提供的其它过程选项可有利地减少与无压缩机选项类似的资本和操作成本,同时减轻与无压缩机选择相关联的较高操作温度和压力相关的风险。 因此,本文公开的方法的实施例包括具有无压缩机设计(低资本和运行成本)的优点的传统设计(具有压缩机的低压力)的最佳特征以及公开的系统独有的其它优点 这里。

    Selective olefin extraction
    10.
    发明授权
    Selective olefin extraction 有权
    选择性烯烃提取

    公开(公告)号:US09409838B2

    公开(公告)日:2016-08-09

    申请号:US14058607

    申请日:2013-10-21

    Abstract: A process and system for separating butenes and butanes by extractive distillation using a polar solvent is disclosed. The process may include: contacting a hydrocarbon mixture including butanes and butenes with a lean solvent mixture in an extractive distillation column to form an enriched solvent fraction comprising butenes; recovering an overheads fraction comprising butanes and a bottoms fraction from the extractive distillation column; feeding the bottoms fraction to a stripper including a stripping section and a wash section; recovering the lean solvent mixture as a bottoms fraction and a stripper overheads fraction comprising butenes and water from the stripper; condensing the overheads fraction to form a water fraction and a product butenes fraction; feeding water as reflux to a top of the stripper wash section; feeding at least a portion of the condensed water fraction intermediate the top and bottom of the stripper wash section as a second reflux.

    Abstract translation: 公开了一种使用极性溶剂通过萃取蒸馏分离丁烯和丁烷的方法和系统。 该方法可以包括:将包含丁烷和丁烯的烃混合物与萃取蒸馏塔中的贫溶剂混合物接触以形成包含丁烯的富集溶剂馏分; 从萃取蒸馏塔回收包含丁烷和塔底馏分的塔顶馏分; 将塔底馏分进料到包括汽提段和洗涤段的汽提塔中; 回收作为底部馏分的贫溶剂混合物和从汽提器中除去含有丁烯和水的汽提塔顶馏分; 冷凝塔顶馏分以形成水分和产物丁烯级分; 将水作为回流进料至脱胶器洗涤部分的顶部; 将至少一部分冷凝水部分作为第二回流供入汽提器洗涤部分的顶部和底部。

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