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公开(公告)号:US10183281B2
公开(公告)日:2019-01-22
申请号:US15341715
申请日:2016-11-02
IPC分类号: B01J27/18 , B01J35/10 , B01J37/03 , B01J37/04 , B01J37/08 , C07C67/03 , C07C67/48 , C07C67/54 , C10L1/02 , B01J21/06 , B01J23/04 , B01J35/00 , C01B25/45 , C07C67/02
摘要: A transesterification catalyst that is heterogeneous and a method for preparing said transesterification catalyst are provided. The catalyst can be used in a variety of transesterification reactor configurations including CSTR (continuous stirred tank reactors), ebullated (or ebullating) beds or any other fluidized bed reactors, and PFR (plug flow, fixed bed reactors). The catalyst can be used for manufacturing commercial grade biodiesel, biolubricants and glycerin.
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公开(公告)号:US10161428B2
公开(公告)日:2018-12-25
申请号:US15720751
申请日:2017-09-29
摘要: A method for facilitating the distribution of the flow of one or more streams within a bed vessel is provided. Disposed within the bed vessel are internal materials and structures including multiple operating zones. One type of operating zone can be a processing zone composed of one or more beds of solid processing material. Another type of operating zone can be a treating zone. Treating zones can facilitate the distribution of the one or more streams fed to processing zones. The distribution can facilitate contact between the feed streams and the processing materials contained in the processing zones.
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公开(公告)号:US11754100B2
公开(公告)日:2023-09-12
申请号:US17509248
申请日:2021-10-25
CPC分类号: F15D1/00 , B01J8/04 , B01J8/0453 , B01J19/30 , B01J2208/0084 , B01J2208/00672 , B01J2208/00938 , B01J2208/025 , B01J2208/027 , B01J2219/30207 , B01J2219/30211 , B01J2219/30215 , B01J2219/30219 , B01J2219/30296 , B01J2219/30416 , B01J2219/30475 , B01J2219/30483 , B01J2219/315
摘要: A method for facilitating the distribution of the flow of one or more streams within a bed vessel is provided. Disposed within the bed vessel are internal materials and structures including multiple operating zones. One type of operating zone can be a processing zone composed of one or more beds of solid processing material. Another type of operating zone can be a treating zone. Treating zones can facilitate the distribution of the one or more streams fed to processing zones. The distribution can facilitate contact between the feed streams and the processing materials contained in the processing zones.
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公开(公告)号:US11052363B1
公开(公告)日:2021-07-06
申请号:US17129488
申请日:2020-12-21
摘要: A method for enabling gas exchange and chemical reactions with one or more liquid streams contained in a reactive process vessel are provided. One or more exchange layers within the process vessel can be composed of both collector media and releaser media. The exchange layers allow elements to facilitate increased performance of vessel operations by promoting gas component mixing and diffusion. Improved rates of gas component exchange mean less coking and more gas components available for reaction.
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公开(公告)号:US10738806B2
公开(公告)日:2020-08-11
申请号:US16379266
申请日:2019-04-09
摘要: A method for facilitating the distribution of the flow of one or more streams within a bed vessel is provided. Disposed within the bed vessel are internal materials and structures including multiple operating zones. One type of operating zone can be a processing zone composed of one or more beds of solid processing material. Another type of operating zone can be a treating zone. Treating zones can facilitate the distribution of the one or more streams fed to processing zones. The distribution can facilitate contact between the feed streams and the processing materials contained in the processing zones.
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公开(公告)号:US10054140B2
公开(公告)日:2018-08-21
申请号:US15676603
申请日:2017-08-14
CPC分类号: F15D1/00 , B01J8/04 , B01J8/0453 , B01J19/30 , B01J2208/00672 , B01J2208/0084 , B01J2208/00938 , B01J2208/025 , B01J2208/027 , B01J2219/30207 , B01J2219/30211 , B01J2219/30215 , B01J2219/30219 , B01J2219/30296 , B01J2219/30416 , B01J2219/30475 , B01J2219/30483 , B01J2219/315
摘要: A method for facilitating the distribution of the flow of one or more streams within a bed vessel is provided. Disposed within the bed vessel are internal materials and structures including multiple operating zones. One type of operating zone can be a processing zone composed of one or more beds of solid processing material. Another type of operating zone can be a treating zone. Treating zones can facilitate the distribution of the one or more streams fed to processing zones. The distribution can facilitate contact between the feed streams and the processing materials contained in the processing zones.
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公开(公告)号:US09643163B2
公开(公告)日:2017-05-09
申请号:US14753623
申请日:2015-06-29
IPC分类号: B01J27/18 , B01J35/10 , B01J37/03 , B01J37/04 , B01J37/08 , C07C67/03 , C07C67/48 , C07C67/54 , C10L1/02 , B01J21/06 , B01J23/04
CPC分类号: B01J27/1806 , B01J21/066 , B01J23/04 , B01J27/18 , B01J35/0006 , B01J35/1014 , B01J35/1057 , B01J35/1061 , B01J37/031 , B01J37/035 , B01J37/036 , B01J37/038 , B01J37/04 , B01J37/08 , C01B25/45 , C07C67/02 , C07C67/03 , C07C67/48 , C07C67/54 , C10L1/026 , Y02E50/13 , Y02P20/582
摘要: A transesterification catalyst that is heterogeneous and a method for preparing said transesterification catalyst are provided. The catalyst can be used in a variety of transesterification reactor configurations including CSTR (continuous stirred tank reactors), ebullated (or ebullating) beds or any other fluidized bed reactors, and PFR (plug flow, fixed bed reactors). The catalyst can be used for manufacturing commercial grade biodiesel, biolubricants and glycerin.
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公开(公告)号:US20160102041A1
公开(公告)日:2016-04-14
申请号:US14753623
申请日:2015-06-29
IPC分类号: C07C67/03 , B01J35/10 , B01J37/03 , C07C67/54 , B01J37/08 , C10L1/02 , C07C67/48 , B01J27/18 , B01J37/04
CPC分类号: B01J27/1806 , B01J21/066 , B01J23/04 , B01J27/18 , B01J35/0006 , B01J35/1014 , B01J35/1057 , B01J35/1061 , B01J37/031 , B01J37/035 , B01J37/036 , B01J37/038 , B01J37/04 , B01J37/08 , C01B25/45 , C07C67/02 , C07C67/03 , C07C67/48 , C07C67/54 , C10L1/026 , Y02E50/13 , Y02P20/582
摘要: A transesterification catalyst that is heterogeneous and a method for preparing said transesterification catalyst are provided. The catalyst can be used in a variety of transesterification reactor configurations including CSTR (continuous stirred tank reactors), ebullated (or ebullating) beds or any other fluidized bed reactors, and PFR (plug flow, fixed bed reactors). The catalyst can be used for manufacturing commercial grade biodiesel, biolubricants and glycerin.
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公开(公告)号:USRE49610E1
公开(公告)日:2023-08-15
申请号:US17019903
申请日:2020-09-14
IPC分类号: C07C67/02 , B01J21/06 , B01J23/04 , B01J27/18 , B01J35/10 , C07C67/03 , C10L1/02 , C10M105/34 , C11C3/00 , B01J37/03 , B01J37/04 , B01J37/08
CPC分类号: C07C67/02 , B01J21/066 , B01J23/04 , B01J27/1806 , B01J35/1014 , B01J35/1057 , B01J35/1061 , C07C67/03 , C10L1/026 , C10M105/34 , C11C3/003 , B01J37/031 , B01J37/036 , B01J37/04 , B01J37/08 , C10L2200/0476 , C10L2270/026 , C10L2290/543 , C10L2290/547 , Y02E50/10 , Y02P20/582 , C07C67/03 , C07C69/52
摘要: A transesterification catalyst that is heterogeneous and a method for preparing said transesterification catalyst are provided. The catalyst can be used in a variety of transesterification reactor configurations including CSTR (continuous stirred tank reactors), ebullated (or ebullating) beds or any other fluidized bed reactors, and PFR (plug flow, fixed bed reactors). The catalyst can be used for manufacturing commercial grade biodiesel, biolubricants and glycerin.
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公开(公告)号:US09770707B2
公开(公告)日:2017-09-26
申请号:US15341736
申请日:2016-11-02
IPC分类号: B01J27/18 , B01J35/10 , B01J37/03 , B01J37/04 , B01J37/08 , C07C67/03 , C07C67/48 , C07C67/54 , C10L1/02 , B01J21/06 , B01J23/04 , B01J35/00 , C01B25/45
CPC分类号: B01J27/1806 , B01J21/066 , B01J23/04 , B01J27/18 , B01J35/0006 , B01J35/1014 , B01J35/1057 , B01J35/1061 , B01J37/031 , B01J37/035 , B01J37/036 , B01J37/038 , B01J37/04 , B01J37/08 , C01B25/45 , C07C67/02 , C07C67/03 , C07C67/48 , C07C67/54 , C10L1/026 , Y02E50/13 , Y02P20/582
摘要: A transesterification catalyst that is heterogeneous and a method for preparing said transesterification catalyst are provided. The catalyst can be used in a variety of transesterification reactor configurations including CSTR (continuous stirred tank reactors), ebullated (or ebullating) beds or any other fluidized bed reactors, and PFR (plug flow, fixed bed reactors). The catalyst can be used for manufacturing commercial grade biodiesel, biolubricants and glycerin.
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