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公开(公告)号:US11230671B2
公开(公告)日:2022-01-25
申请号:US17028994
申请日:2020-09-22
发明人: Xingying Lan , Yuming Zhang , Jinsen Gao , Xiaogang Shi , Chengxiu Wang
IPC分类号: B01J8/00 , B01J8/18 , B01J8/26 , B01J8/28 , B01J19/00 , B01J19/24 , C10G9/36 , C10G31/08 , C10G57/00
摘要: A coupling reaction apparatus for heavy oil cracking-gasification, including a cracking section and a gasification section communicated with each other, and the cracking section is located above the gasification section; the cracking section is provided with a heavy oil raw material inlet and a fluidizing gas inlet, and an upper part of the cracking section is provided with an oil-gas outlet; and the gasification section is provided with a gasification agent inlet.
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公开(公告)号:US20150210941A1
公开(公告)日:2015-07-30
申请号:US14684196
申请日:2015-04-10
发明人: TIANZHEN HAO , Jinsen Gao , Dezhong Li , Liang Zhao , Zhiyuan Lu , Xingying Lan
CPC分类号: C10G67/04 , C10G21/14 , C10G21/16 , C10G21/20 , C10G21/22 , C10G21/28 , C10G53/16 , C10G67/16 , C10G2300/202 , C10G2400/02
摘要: The present invention provides a process for desulfurizing gasoline fraction by solvent extraction: introducing the gasoline fraction into an extraction tower at a lower-middle part thereof, introducing a solvent into the extraction tower at the top thereof, injecting saturated C5 hydrocarbon into a reflux device at the bottom of the extraction tower, wherein the gasoline fraction which is desulfurized flows out from the top of the extraction tower; the solvent that has extracted sulfide, aromatics and C5 hydrocarbon flows out from the bottom of the extraction tower, and is separated into a C5 hydrocarbon-containing light component, a sulfur-rich component, water and the solvent. The present invention also provides a process for deeply desulfurizing catalytic cracking gasoline, which flexibly combines the process described above and an existing desulfurization technology.
摘要翻译: 本发明提供了一种通过溶剂萃取法将汽油馏分脱硫的方法:将汽油馏分引入到其中下部的萃取塔中,将溶剂引入塔顶部的萃取塔中,将饱和C 5烃注入回流装置 在提取塔的底部,其中脱硫的汽油馏分从萃取塔的顶部流出; 提取硫化物,芳烃和C5烃的溶剂从萃取塔底部流出,分离成含C5烃的轻组分,富含硫的组分,水和溶剂。 本发明还提供了一种深度脱硫催化裂化汽油的方法,其灵活地组合了上述方法和现有的脱硫技术。
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3.
公开(公告)号:US11370978B2
公开(公告)日:2022-06-28
申请号:US17028896
申请日:2020-09-22
发明人: Yuming Zhang , Jinsen Gao , Xingying Lan , Chengxiu Wang , Xiaogang Shi
摘要: The present disclosure provides a method and an apparatus for integrating pressurized hydrocracking of heavy oil and coke gasification. A coupled reactor having a cracking section and a gasification section is used in the method: a heavy oil feedstock and a hydrogenation catalyst are fed into a cracking section, to generate light oil-gas and coke; the coke is carried by the coke powder into the gasification section, to generate syngas; a regenerated coke powder is returned to the cracking section; the syngas enters the cracking section and merges with light oil-gas, and enters a gas-solid separator, to separate out first-stage solid particles and second-stage particles in sequence, and a purified oil-gas product is collected; oil-gas fractionation of the purified oil-gas product is performed, and a light oil product and a syngas product are collected. Yield and quality of the light oil can be improved by the method.
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公开(公告)号:US11230677B2
公开(公告)日:2022-01-25
申请号:US17028957
申请日:2020-09-22
发明人: Jinsen Gao , Yuming Zhang , Xingying Lan , Chengxiu Wang , Xiaogang Shi
摘要: A method for heavy oil lightening and synthesis gas production and a device thereof are provided, where the method uses a cracking/gasification coupled reactor, which internally has a cracking section and a gasification section that communicate with each other, and includes the following steps: feeding a heavy oil material into the cracking section to implement a cracking reaction, to produce a light oil gas and a coke; the coke being carried by the coke powders and descending into the gasification section to implement a gasification reaction, to produce a synthesis gas; at least performing a first stage gas-solid separation, collecting coke powder particles and dividing them into two parts; performing an oil and gas fractionation on a purified oil and gas product output by the gas-solid separation system, and collecting a light oil product and a synthesis gas product.
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5.
公开(公告)号:US11230678B2
公开(公告)日:2022-01-25
申请号:US17028980
申请日:2020-09-22
发明人: Xingying Lan , Yuming Zhang , Jinsen Gao , Chengxiu Wang , Xiaogang Shi
摘要: An integrated method and an integrated device for heavy oil contact lightening and coke gasification are provided. The integrated method uses a coupled reactor including a cracking section and a gasification section, and the integrated method includes: feeding a heavy oil material into the cracking section to implement a cracking reaction, to obtain a light oil gas and a carbon-deposited contact agent; passing the carbon-deposited contact agent into the gasification section, so as to implement a gasification reaction, to obtain a regenerated contact agent and a syngas; and discharging the light oil gas and the ascended and incorporated syngas from the cracking section, to perform a gas-solid separation, so that the carbon-deposited contact agent carried is separated and returned to the cracking section, and a purified oil gas is obtained at the same time.
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6.
公开(公告)号:US11230674B2
公开(公告)日:2022-01-25
申请号:US17028930
申请日:2020-09-22
发明人: Xingying Lan , Yuming Zhang , Jinsen Gao , Chengxiu Wang
摘要: The present disclosure provides an integrated method and apparatus for catalytic cracking of heavy oil and production of syngas. A cracking-gasification coupled reactor having a cracking section and a gasification section is used as a reactor in the method. A heavy oil feedstock is fed into a cracking section to contact with a bed material in a fluidized state that contains a cracking catalyst, a catalytic cracking reaction is conducted under atmospheric pressure to obtain light oil-gas and coke. The coke is carried downward by the bed material into a gasification section to conduct a gasification reaction to generate syngas; the syngas goes upward into the cracking section to merge with the light oil-gas, and is guided out from the coupled reactor and enter a gas-solid separation system. Oil-gas fractionation is performed to a purified oil-gas product output from the gas-solid separation system to collect light oil and syngas products.
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公开(公告)号:US09856423B2
公开(公告)日:2018-01-02
申请号:US14684196
申请日:2015-04-10
发明人: Tianzhen Hao , Jinsen Gao , Dezhong Li , Liang Zhao , Zhiyuan Lu , Xingying Lan
IPC分类号: C10G67/04 , C10G21/28 , C10G21/14 , C10G21/16 , C10G21/22 , C10G21/20 , C10G53/16 , C10G67/16
CPC分类号: C10G67/04 , C10G21/14 , C10G21/16 , C10G21/20 , C10G21/22 , C10G21/28 , C10G53/16 , C10G67/16 , C10G2300/202 , C10G2400/02
摘要: The present invention provides a process for desulfurizing gasoline fraction by solvent extraction: introducing the gasoline fraction into an extraction tower at a lower-middle part thereof, introducing a solvent into the extraction tower at the top thereof, injecting saturated C5 hydrocarbon into a reflux device at the bottom of the extraction tower, wherein the gasoline fraction which is desulfurized flows out from the top of the extraction tower; the solvent that has extracted sulfide, aromatics and C5 hydrocarbon flows out from the bottom of the extraction tower, and is separated into a C5 hydrocarbon-containing light component, a sulfur-rich component, water and the solvent. The present invention also provides a process for deeply desulfurizing catalytic cracking gasoline, which flexibly combines the process described above and an existing desulfurization technology.
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