CATALYTIC CRACKER Russian patent published in 2024 - IPC C10G11/18 B01J8/24 

Abstract RU 2811276 C1

FIELD: oil refining; petrochemical industry.

SUBSTANCE: invention concerns catalytic cracking unit (1), including series-connected riser reactor (2), separation unit (3), catalyst stripping unit (21), and catalyst regenerator (4). Riser reactor (2) includes a sequentially located regulated input unit (5) of transport gas, including water vapor, input unit (b) of hot catalyst, with the possibility of supplying a hot catalyst from the outlet of catalyst regenerator (4), initial reaction section (7), unit for controlled input (8) of raw materials, main reaction section (9), first unit for controlled input (10) of cooling recirculating hydrocarbon distillate fractions, end reaction section (11). Separation unit (3) is located at the exit from end reaction section (11) of lift reactor (2) and includes separator (12) equipped with inlet (13), drain risers (14), and gas outlet pipes (15), while inlet hole (13) connected to the outlet of end reaction section (11) of elevator reactor (2), cyclones (16), each equipped with inlet pipe (17), gas outlet pipe (18), and drain riser (19), with inlet pipes (17) cyclones (16) are located at the outlet of gas outlet pipes (15) of separator (12) with the possibility of a mixture of cracking product vapours and water vapour entering from gas outlet pipes (15) of separator (12) into inlet pipes (17) of cyclones (16), and gas outlet pipes (18) of cyclones (16) are configured to output target products, second controlled input unit (20) of recirculating hydrocarbon distillate fractions, made with the possibility of controlled input of cooling recirculating hydrocarbon distillate fractions directly to the outlet from gas outlet pipes (15) of separator ( 12) before entering inlet pipes (17) of cyclones (16). Catalyst stripping unit (21), located under drain risers (14) of separator (12) and drain risers (19) of cyclones (16), is equipped with catalyst output unit (22), which is connected to the inlet of catalyst regenerator (4).

EFFECT: increased severity of ongoing processes while simultaneously increasing the yield of target products and reducing the proportion of undesirable secondary reactions.

4 cl, 4 dwg, 1 ex

Similar patents RU2811276C1

Title Year Author Number
CATALYTIC CRACKING METHOD 2023
  • Andreev Boris Vladimirovich
  • Basov Rostislav Vladimirovich
  • Ustinov Andrej Stanislavovich
  • Belyavskij Oleg Germanovich
  • Glazov Aleksandr Vitalevich
  • Senov Andrej Sergeevich
RU2811274C1
PROCEDURE FOR CATALYTIC CRACKING OF HYDROCARBON MATERIAL WITH YIELD OF LIGHT OLEFINS AND DEVICE FOR ITS IMPLEMENTATION 2012
  • Soljar Boris Zakharovich
  • Glazov Leonid Shaevich
  • Mnev Maksim Vladimirovich
  • Klimtseva Elena Ar'Evna
  • Liberzon Isaak Meerovich
  • Aladysheva Ehlmira Zarifovna
RU2487160C1
METHOD AND INSTALLATION OF FLUID CATALYTIC CRACKING FOR MAXIMUM INCREASE IN YIELD OF LIGHT OLEFINS AND OTHER APPLICATIONS 2020
  • Chen, Liang
  • Loezos, Peter
  • Marri, Rama, Rao
  • Tomsula, Bryan
  • Hood, Jon, A.
  • Singh, Hardik
  • Dorsey, Michael
  • Breckenridge, Justin
RU2811472C2
METHOD OF CATALYTIC CRACKING OF HYDROCARBON RAW MATERIAL AND DEVICE FOR ITS IMPLEMENTATION 2009
  • Soljar Boris Zakharovich
  • Glazov Leonid Shaevich
  • Klimtseva Elena Ar'Evna
  • Liberzon Isaak Meerovich
  • Aladysheva Ehlmira Zarifovna
RU2410412C1
OIL STOCK PROCESSING METHOD 2001
  • Murtazin F.R.
  • Ivashchenko A.A.
  • Bashirov R.F.
  • Shein V.P.
  • Zhirnov B.S.
RU2202592C1
EQUIPMENT AND METHOD OF CATALYTIC CRACKING 2010
  • Xie Chaogang
  • Gao Yongcan
  • Lu Weimin
  • Long Jun
  • Gui Yan
  • Zhang Jiushun
  • Yang Yinan
  • Ma Jianguo
  • Li Zheng
  • Jiang Nan
RU2535675C2
METHOD AND APPARATUS FOR CATALYTIC CRACKING FOR PRODUCING PROPYLENE 2012
  • Gao Yongcan
  • Xie Chaogang
  • Lu Weimin
  • Zhu Jinquan
  • Cui Yan
  • Zhang Jiushun
  • Yang Yinan
  • Sha Youxin
  • Ma Jianguo
RU2580829C2
METHOD OF DESTRUCTIVE ADSORPTION PROCESSING OF HEAVY OIL RESIDUES AND DEVICE FOR REALIZATION OF THIS METHOD 2004
  • Akhmetov Safa Akhmetovich
  • Akhmetov Salavat Safaevich
  • Galimov Robert Rashitovich
  • Ishmijarov Marat Khafizovich
RU2280674C2
PLANT AND METHOD OF PRODUCING MEDIUM DISTILLATE AND LOWER OLEFINS FROM HYDROCARBON RAW STOCK 2008
  • Khadzhidzhordzh Dzhordzh A.
  • Mo Vejdzhian
  • Shaverin Kolin Dzhon
RU2452762C2
METHOD OF CONVERTING HYDROCARBON STREAM AND, OPTIONALLY, OBTAINING PROCESSED DISTILLATE PRODUCT 2013
  • Sehdler Klejton K.
  • Gozling Kristofer D.
RU2565048C1

RU 2 811 276 C1

Authors

Andreev Boris Vladimirovich

Basov Rostislav Vladimirovich

Ustinov Andrej Stanislavovich

Belyavskij Oleg Germanovich

Glazov Aleksandr Vitalevich

Senov Andrej Sergeevich

Dates

2024-01-11Published

2023-01-09Filed