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公开(公告)号:US20190233284A1
公开(公告)日:2019-08-01
申请号:US16344776
申请日:2017-10-25
申请人: TECHNIP FRANCE
CPC分类号: C01B3/384 , B01J8/0257 , B01J8/062 , B01J2208/00176 , B01J2208/00194 , B01J2208/00221 , B01J2208/00504 , B01J2208/0053 , B01J2208/00539 , B01J2208/00557 , B01J2208/00752 , B01J2208/00761 , B01J2208/0092 , B01J2208/065 , B01J2219/00024 , B01J2219/19 , B01J2219/1923 , B01J2219/1928 , C01B3/38
摘要: The inventions is directed to a new design for catalyst tubes, which makes it possible to apply the concept of regenerative reforming into steam reformers having catalyst tube inlets and outlets at opposite sides of the furnace chamber. The catalyst tube comprises an inlet for process gas to enter the catalyst tube and an outlet for process gas to exit the catalyst tube, which inlet and outlet are located at opposite ends of the catalyst tube. The catalyst tube further comprises a first annular channel comprising the catalyst, a second annular channel for process gas to flow countercurrently or co-currently to the process gas flowing through the first annular channel.
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公开(公告)号:US20150093577A1
公开(公告)日:2015-04-02
申请号:US14504295
申请日:2014-10-01
发明人: Liang-Shih Fan , Fanxing Li
IPC分类号: C01B3/34
CPC分类号: C10J3/725 , B01J19/245 , B01J2219/19 , B01J2219/24 , C01B3/02 , C01B3/344 , C10J3/12 , C10J3/463 , C10J3/485 , C10J2300/0916 , C10J2300/093 , C10J2300/0943 , C10J2300/0959 , C10J2300/0969 , C10J2300/0976 , C10J2300/1671 , C10J2300/1807 , C10J2300/1869 , C10J2300/1884 , F23C99/00 , F23C2900/99008 , Y02E20/16 , Y02E20/346 , Y02P20/52 , Y10T428/2982
摘要: A system for converting fuel is provided and includes a first reactor comprising a plurality of ceramic composite particles, the ceramic composite particles comprising at least one metal oxide disposed on a support, wherein the first reactor is configured to reduce the at least one metal oxide with a fuel to produce a reduced metal or a reduced metal oxide; a second reactor configured to oxidize at least a portion of the reduced metal or reduced metal oxide from the said first reactor to produce a metal oxide intermediate; a source of air; and a third reactor communicating with said source of air and configured to regenerate the at least one metal oxide from the remaining portion of the solids discharged from the said first reactor and the solids discharged from the said second reactor by oxidizing the metal oxide intermediate.
摘要翻译: 提供了用于转化燃料的系统,并且包括包含多个陶瓷复合颗粒的第一反应器,所述陶瓷复合颗粒包含设置在载体上的至少一种金属氧化物,其中所述第一反应器构造成用至少一种金属氧化物还原所述至少一种金属氧化物 产生还原金属或还原金属氧化物的燃料; 第二反应器,被配置为从所述第一反应器氧化至少一部分还原金属或还原的金属氧化物以产生金属氧化物中间体; 空气来源 以及第三反应器,其与所述空气源连通并且被配置为从所述第一反应器排出的固体的剩余部分和通过氧化金属氧化物中间体从所述第二反应器排出的固体再生至少一种金属氧化物。
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公开(公告)号:US20110176968A1
公开(公告)日:2011-07-21
申请号:US13121009
申请日:2009-09-28
申请人: Liang-Shih Fan , Li Fanxing
发明人: Liang-Shih Fan , Li Fanxing
CPC分类号: C10J3/725 , B01J19/245 , B01J2219/19 , B01J2219/24 , C01B3/02 , C01B3/344 , C10J3/12 , C10J3/463 , C10J3/485 , C10J2300/0916 , C10J2300/093 , C10J2300/0943 , C10J2300/0959 , C10J2300/0969 , C10J2300/0976 , C10J2300/1671 , C10J2300/1807 , C10J2300/1869 , C10J2300/1884 , F23C99/00 , F23C2900/99008 , Y02E20/16 , Y02E20/346 , Y02P20/52 , Y10T428/2982
摘要: A system for converting fuel is provided and includes a first reactor comprising a plurality of ceramic composite particles, the ceramic composite particles comprising at least one metal oxide disposed on a support, wherein the first reactor is configured to reduce the at least one metal oxide with a fuel to produce a reduced metal or a reduced metal oxide; a second reactor configured to oxidize at least a portion of the reduced metal or reduced metal oxide from the said first reactor to produce a metal oxide intermediate; a source of air; and a third reactor communicating with said source of air and configured to regenerate the at least one metal oxide from the remaining portion of the solids discharged from the said first reactor and the solids discharged from the said second reactor by oxidizing the metal oxide intermediate.
摘要翻译: 提供了用于转化燃料的系统,并且包括包含多个陶瓷复合颗粒的第一反应器,所述陶瓷复合颗粒包含设置在载体上的至少一种金属氧化物,其中所述第一反应器构造成用至少一种金属氧化物还原所述至少一种金属氧化物 用于生产还原金属或还原金属氧化物的燃料; 第二反应器,被配置为从所述第一反应器氧化至少一部分还原金属或还原的金属氧化物以产生金属氧化物中间体; 空气来源 以及第三反应器,其与所述空气源连通并且被配置为从所述第一反应器排出的固体的剩余部分和通过氧化金属氧化物中间体从所述第二反应器排出的固体再生至少一种金属氧化物。
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公开(公告)号:US09315386B2
公开(公告)日:2016-04-19
申请号:US14366366
申请日:2012-11-28
申请人: Vladimir Zalmanovich Mordkovich , Aida Razimovna Karaeva , Maxim Alexandrovich Khaskov , Eduard Borisovich Mitberg
发明人: Vladimir Zalmanovich Mordkovich , Aida Razimovna Karaeva , Maxim Alexandrovich Khaskov , Eduard Borisovich Mitberg
CPC分类号: C01B31/0233 , B01J19/2415 , B01J2219/00166 , B01J2219/19 , B82Y30/00 , B82Y40/00 , C01B32/162 , C01B32/164 , C01B2202/34
摘要: The present invention is used to produce long carbon nanotubes used, for example, in automobile and/or aircraft industry. An object of the invention is to obtain bundles of multi-walled and well oriented nanotubes of sufficient length and provide stability of continuous nanotubes producing process. The method comprises introducing a carbon-bearing component, a promoter and a precursor of a carbon nanotube growth catalyst in a carrier gas stream to form a mixture of these components; passing said mixture through the a reactor heated to an operating temperature of 1000° C. to 1200° C. and removing nanotubes formed in the reactor into a product receiver. The mixture is fed in the reactor from the bottom upwards at a linear flow velocity of 50 mm/c to 130 mm/c. When the temperature in the reactor reaches said operating temperature, the linear flow velocity of the mixture is decreased to 4-10 mm/c, and the linear flow velocity is increased to 30-130 mm/c at the outlet of the reactor. The apparatus comprises means for introducing the carbon-bearing component, the promoter and the precursor of the carbon nanotube growth catalyst in the carrier gas stream, a vertical reactor with a working chamber, means for heating the working chamber to the operating temperature, means for delivering the mixture to the working chamber of the reactor and means for removing products from the working chamber. The chamber is made of three successive sections, namely a lower inlet 16 section, a middle 17 section and an upper outlet 18 section and the diameter of the lower section 16 is ⅕ to ⅓ of the diameter of the middle section 17, while the diameter of the upper section 18 is from ¼ to ⅓ of the diameter of the middle section 17.
摘要翻译: 本发明用于生产例如汽车和/或飞机工业中使用的长碳纳米管。 本发明的目的是获得具有足够长度的多壁和良好取向的纳米管束并提供连续的纳米管生产方法的稳定性。 该方法包括在载气流中引入碳载体组分,促进剂和碳纳米管生长催化剂的前体以形成这些组分的混合物; 将所述混合物通过加热至1000℃至1200℃的操作温度的反应器,并将形成在反应器中的纳米颗粒除去产品接收器。 将混合物从底部向上以50mm / c至130mm / c的线性流速进料到反应器中。 当反应器中的温度达到所述工作温度时,混合物的线性流速降低到4-10mm / c,在反应器出口处线性流速增加到30-130mm / c。 该装置包括用于将载气组分,促进剂和碳纳米管生长催化剂的前体引入载气流的装置,具有工作室的垂直反应器,用于将工作室加热至工作温度的装置, 将混合物输送到反应器的工作室,以及用于从工作室中除去产物的装置。 该室由三个连续的部分制成,即下部入口16部分,中部17部分和上部出口18部分,下部部分16的直径为中间部分17的直径的¼至1/3,而直径 上部18的直径为中间部分17的直径的1/4到1/3。
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公开(公告)号:US08877147B2
公开(公告)日:2014-11-04
申请号:US13121009
申请日:2009-09-28
申请人: Liang-shih Fan , Fanxing Li
发明人: Liang-shih Fan , Fanxing Li
IPC分类号: B01J8/00 , F23C99/00 , C10J3/46 , C10J3/72 , C10J3/12 , B01J8/18 , B01J7/00 , B01J19/00 , B01J23/00 , B01J35/00 , B01J35/02
CPC分类号: C10J3/725 , B01J19/245 , B01J2219/19 , B01J2219/24 , C01B3/02 , C01B3/344 , C10J3/12 , C10J3/463 , C10J3/485 , C10J2300/0916 , C10J2300/093 , C10J2300/0943 , C10J2300/0959 , C10J2300/0969 , C10J2300/0976 , C10J2300/1671 , C10J2300/1807 , C10J2300/1869 , C10J2300/1884 , F23C99/00 , F23C2900/99008 , Y02E20/16 , Y02E20/346 , Y02P20/52 , Y10T428/2982
摘要: A system for converting fuel is provided and includes a first reactor comprising a plurality of ceramic composite particles, the ceramic composite particles comprising at least one metal oxide disposed on a support, wherein the first reactor is configured to reduce the at least one metal oxide with a fuel to produce a reduced metal or a reduced metal oxide; a second reactor configured to oxidize at least a portion of the reduced metal or reduced metal oxide from the said first reactor to produce a metal oxide intermediate; a source of air; and a third reactor communicating with said source of air and configured to regenerate the at least one metal oxide from the remaining portion of the solids discharged from the said first reactor and the solids discharged from the said second reactor by oxidizing the metal oxide intermediate.
摘要翻译: 提供了用于转化燃料的系统,并且包括包含多个陶瓷复合颗粒的第一反应器,所述陶瓷复合颗粒包含设置在载体上的至少一种金属氧化物,其中所述第一反应器构造成用至少一种金属氧化物还原所述至少一种金属氧化物 产生还原金属或还原金属氧化物的燃料; 第二反应器,被配置为从所述第一反应器氧化至少一部分还原金属或还原的金属氧化物以产生金属氧化物中间体; 空气来源 以及第三反应器,其与所述空气源连通并且被配置为从所述第一反应器排出的固体的剩余部分和通过氧化金属氧化物中间体从所述第二反应器排出的固体再生至少一种金属氧化物。
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公开(公告)号:US20230272295A1
公开(公告)日:2023-08-31
申请号:US18016418
申请日:2021-07-19
CPC分类号: C10K3/008 , C10J3/64 , C10J3/84 , B01J19/126 , H05H1/4622 , B01J12/002 , B01J19/088 , C10J2300/0916 , C10J2300/1603 , H05H2245/10 , B01J2219/19
摘要: A plasma processing method for a gas comprises supplying a gas inside a cavity for plasma processing, supplying microwaves having a predetermined frequency and power in order to generate a plasma of the gas, and propagating the microwaves in the gas by means of a waveguide which communicates directly with the cavity so as to provide a plasma cracking processing operation for the gas inside the cavity (2).
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公开(公告)号:US20180036708A1
公开(公告)日:2018-02-08
申请号:US15665912
申请日:2017-08-01
IPC分类号: B01J19/24 , C08L23/12 , C08L23/14 , C08F210/06
CPC分类号: B01J19/242 , B01J8/003 , B01J8/1827 , B01J8/20 , B01J8/245 , B01J8/26 , B01J8/28 , B01J8/34 , B01J8/382 , B01J2208/00274 , B01J2208/0084 , B01J2208/00902 , B01J2219/185 , B01J2219/19 , B01J2231/122 , C08F210/06 , C08L23/12 , C08L23/14 , C08L2205/02 , C08L2207/02 , C08F2/34 , C08F2/001 , C08F4/6548 , C08F110/06 , C08F4/6492 , C08F10/00 , C08F4/651 , C08F2/01 , C08F210/16 , C08F2500/17
摘要: Provided are a system for producing a polyolefin, a method of producing a polyolefin, and a method of producing a heterophasic propylene polymer material, each of which allows (i) a gel, to be contained in a molded product that is made of an obtained polyolefin, to be reduced and (ii) a polyolefin to be continuously produced stably. A polyolefin producing system (1) includes: a cylindrical member which extends in a vertical direction; diameter decreasing members each of which is provided to the cylindrical member, each of the diameter decreasing members having (i) an inner diameter that decreases as the each of the diameter decreasing members extends downward and (ii) a gas inlet opening at a lower end of the each of the diameter decreasing members; spouted bed type olefin polymerization reaction regions (25) each of which is surrounded by (a) an inner surface of a corresponding one of the diameter decreasing members and (b) part of an inner surface of the cylindrical member which part extends upward from the corresponding one of the diameter decreasing members, each of the spouted bed type olefin polymerization reaction regions (25) being a region in which a spouted bed is formed, the number of the spouted bed type olefin polymerization reaction regions (25) being 3 or more; and at least one fluidized bed type olefin polymerization reaction region which is provided at a stage subsequent to the spouted bed type olefin polymerization reaction regions (25).
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公开(公告)号:US3687635A
公开(公告)日:1972-08-29
申请号:US3687635D
申请日:1970-08-13
申请人: ELECTROLUX AB
发明人: WIJARD ENDEL , ODSVALL JAN
CPC分类号: B01J3/04 , B01J2219/187 , B01J2219/19
摘要: AN AUTOCLAVE DEVICE PROVIDED WITH DIFFERENT PRESSURE CHAMBERS BETWEEN WHICH GOODS TO BE TREATED CAN BE TRANSFERRED IN A PREETERMINED DIRECTION OF FLOW WITHOUT THE NECESSITY OF EQUALIZING THE PRESSURE DURING THE TREATMENT IN ONE CHAMBER TO AMBIENT ATMOSPHERIC PRESSURE BEFORE TRASFERRING THE GOODS TO A NEXT CHAMBER. THIS NEW DEVICE ENABLES AN AUTOCLAVE PROCESS TO BE PERFORMED CONTINUOUSLY AND EVEN AUTOMATICALLY WITH CONSIDERABLE SAVINGS IN STEAM CONSUMPTION.
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公开(公告)号:US10081772B2
公开(公告)日:2018-09-25
申请号:US15191249
申请日:2016-06-23
发明人: Liang-Shih Fan , Fanxing Li
IPC分类号: B01J19/00 , B01J19/24 , C01B3/02 , C01B3/34 , C10J3/12 , C10J3/46 , C10J3/48 , C10J3/72 , F23C99/00
CPC分类号: C10J3/725 , B01J19/245 , B01J2219/19 , B01J2219/24 , C01B3/02 , C01B3/344 , C10J3/12 , C10J3/463 , C10J3/485 , C10J2300/0916 , C10J2300/093 , C10J2300/0943 , C10J2300/0959 , C10J2300/0969 , C10J2300/0976 , C10J2300/1671 , C10J2300/1807 , C10J2300/1869 , C10J2300/1884 , F23C99/00 , F23C2900/99008 , Y02E20/16 , Y02E20/346 , Y02P20/52 , Y10T428/2982
摘要: A system for converting fuel is provided and includes a first reactor comprising a plurality of ceramic composite particles, the ceramic composite particles comprising at least one metal oxide disposed on a support, wherein the first reactor is configured to reduce the at least one metal oxide with a fuel to produce a reduced metal or a reduced metal oxide; a second and reactor configured to oxidize at least a portion of the reduced metal or reduced metal oxide from the said first reactor to produce a metal oxide intermediate; a source of air; and a third reactor communicating with said source of air and configured to regenerate the at least one metal oxide from the remaining portion of the solids discharged from the said first reactor and the solids discharged from the said second reactor for by oxidizing the metal oxide intermediate.
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10.
公开(公告)号:US20180179081A1
公开(公告)日:2018-06-28
申请号:US15735441
申请日:2016-06-10
申请人: Areva NC
发明人: Alex Jourdan , Marc Dupoizat
CPC分类号: C01G43/01 , B01D39/2027 , B01D45/08 , B01D49/003 , B01D50/002 , B01J4/002 , B01J6/008 , B01J19/24 , B01J19/26 , B01J2219/00157 , B01J2219/19 , B01J2219/1946 , C01P2006/12 , C01P2006/80 , C01P2006/82
摘要: An apparatus (1) for thermal denitration of a uranyl nitrate hydrate to uranium trioxide UO3. The apparatus (1) comprises a burner (114) and a reaction chamber (110) configured to carry out thermal denitration of uranyl nitrate hydrate and to form uranium trioxide UO3 in the form of particles. The apparatus also comprises a separating chamber (120) suitable for separating UO3 particles from the gases resulting from the thermal denitration carried out in the reaction chamber (110), and at least one filter (130) configured for purifying the gases. The separating chamber (120) is a decanting chamber into which the reaction chamber (110) directly opens out. The filter (130) is capable of performing the separation at a temperature greater than or equal to 350° C. The invention also relates to use of such an apparatus, to a thermal denitration process and to UO3 particles obtained by such a process.
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