SG10201709746QA - Impact-Reducing Uniform-Flowing Disc and Reactor - Google Patents
Impact-Reducing Uniform-Flowing Disc and ReactorInfo
- Publication number
- SG10201709746QA SG10201709746QA SG10201709746QA SG10201709746QA SG10201709746QA SG 10201709746Q A SG10201709746Q A SG 10201709746QA SG 10201709746Q A SG10201709746Q A SG 10201709746QA SG 10201709746Q A SG10201709746Q A SG 10201709746QA SG 10201709746Q A SG10201709746Q A SG 10201709746QA
- Authority
- SG
- Singapore
- Prior art keywords
- impact
- falling
- reducing
- tower tray
- uniform
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/72—Controlling or regulating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/0278—Feeding reactive fluids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
- B01J19/006—Baffles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/2415—Tubular reactors
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J4/00—Feed or outlet devices; Feed or outlet control devices
- B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
- B01J8/0446—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
- B01J8/0449—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds
- B01J8/0453—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds the beds being superimposed one above the other
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
- B01J8/0492—Feeding reactive fluids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00796—Details of the reactor or of the particulate material
- B01J2208/00893—Feeding means for the reactants
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00796—Details of the reactor or of the particulate material
- B01J2208/00893—Feeding means for the reactants
- B01J2208/00929—Provided with baffles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00796—Details of the reactor or of the particulate material
- B01J2208/00938—Flow distribution elements
Abstract
The present invention relates to the chemical processing equipment field, and discloses an impact-reducing uniform-flowing disc and a reactor. The impact-reducing uniform-flowing disc comprises a tower tray (), a material falling pipe (200) penetrating through the tower tray 5 (100), and an impact-reducing device (300) configured to buffer the kinetic energy of an obliquely falling material flow, wherein, the impact-reducing device (300) has a guide surface configured to guide the obliquely falling material flow to flow along the guide surface and fall to the tower tray (100), and overflow holes (201) are arranged at a portion of the material falling pipe (200) above the tower tray (100), and wherein, the impact-reducing uniform-flowing disc 10 comprises a plurality of the material falling pipes (200) and a plurality of the impact-reducing devices (300) configured to provide a buffering falling material function for the plurality of material falling pipes (200). With the impact-reducing device, the kinetic energy of the material flow can be buffered, a falling material stream can be formed, and uneven material distribution incurred by any error of levelness of the tower tray can be avoided. In addition, the device 15 provided in the present invention eliminates the impact force generated by residual kinetic energy, and avoids a "wave pushing" phenomenon. Figure 1 20 36
Applications Claiming Priority (9)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201611052855.4A CN108097178B (en) | 2016-11-25 | 2016-11-25 | Tooth weir type impact reduction and flow equalization disc |
CN201611051739.0A CN108097176B (en) | 2016-11-25 | 2016-11-25 | Ring plate type impact reducing and flow equalizing disc |
CN201611083262.4A CN108114668B (en) | 2016-11-25 | 2016-11-25 | Baffle type impact-reducing flow-equalizing disc |
CN201611084902.3A CN108114671B (en) | 2016-11-25 | 2016-11-25 | Flanging type impact-reducing flow-equalizing disc |
CN201611052869.6A CN108097179B (en) | 2016-11-25 | 2016-11-25 | Grid type impact-reducing flow-equalizing disc |
CN201611051740.3A CN108097177B (en) | 2016-11-25 | 2016-11-25 | Impact-reducing flow-equalizing disc with scale depositing function |
CN201611084901.9A CN108114670B (en) | 2016-11-30 | 2016-11-30 | Sleeve type impact reducing and flow equalizing disc |
CN201611083960.4A CN108114669B (en) | 2016-11-25 | 2016-11-30 | Baffle type impact-reducing flow-equalizing disc |
CN201611083261.XA CN108114667B (en) | 2016-11-25 | 2016-11-30 | Edge-folding type injection disc |
Publications (1)
Publication Number | Publication Date |
---|---|
SG10201709746QA true SG10201709746QA (en) | 2018-06-28 |
Family
ID=60950643
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SG10201709746QA SG10201709746QA (en) | 2016-11-25 | 2017-11-24 | Impact-Reducing Uniform-Flowing Disc and Reactor |
Country Status (5)
Country | Link |
---|---|
KR (1) | KR101989328B1 (en) |
GB (1) | GB2560066B (en) |
RU (1) | RU2672742C1 (en) |
SG (1) | SG10201709746QA (en) |
TW (1) | TWI664021B (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2022138286A1 (en) * | 2020-12-21 | 2022-06-30 | 昭和電工株式会社 | Fixed-bed reactor |
CN113842840A (en) * | 2021-10-26 | 2021-12-28 | 中国石油化工股份有限公司 | Tubular gas-liquid distributor |
Family Cites Families (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1475082A (en) * | 1973-05-16 | 1977-06-01 | Shell Int Research | Process and apparatus for the catalyric treatment of materials containing solid contaminants |
SU1098559A1 (en) * | 1983-07-01 | 1984-06-23 | Всесоюзный Научно-Исследовательский И Проектно-Конструкторский Институт Нефтяного Машиностроения | Petroleum distillate processing reactor |
US5635145A (en) * | 1994-08-23 | 1997-06-03 | Shell Oil Company | Multi-bed downflow reactor |
US6221133B1 (en) * | 1999-12-29 | 2001-04-24 | Norton Chemical Process Products Corporation | Fluid separation packing |
CA2535987C (en) * | 2003-08-18 | 2012-05-22 | Shell Internationale Research Maatschappij B.V. | Distribution device |
MY142153A (en) * | 2004-12-10 | 2010-09-30 | Shell Int Research | Reactor tube apparatus |
DE602006000497D1 (en) * | 2005-05-13 | 2008-03-20 | Haldor Topsoe As | Distributor device for downflow reactors with at least one compartmentalized chimney stack |
FR2889973B1 (en) * | 2005-08-26 | 2007-11-09 | Inst Francais Du Petrole | FILTER TRAY FOR COIL BED REACTOR CURRENT DESCENDING LIQUID GAS |
KR101122813B1 (en) * | 2006-08-30 | 2012-03-21 | 유오피 엘엘씨 | Apparatus and process for distributing liquid |
CN101279229B (en) * | 2007-04-04 | 2011-02-09 | 中国石油化工股份有限公司上海石油化工研究院 | Trickle bed reactor |
US8377386B2 (en) * | 2008-03-07 | 2013-02-19 | Haldor Topsoe A/S | Catalytic reactor |
US8409521B2 (en) * | 2008-08-13 | 2013-04-02 | Air Products And Chemicals, Inc. | Tubular reactor with jet impingement heat transfer |
FR2982172B1 (en) * | 2011-11-03 | 2013-11-01 | Ifp Energies Now | DISTRIBUTION TRAY OF A LIQUID GAS MIXTURE EQUIPPED WITH DISTRIBUTION ELEMENTS THAT ARE LITTLE SUSCEPTIBLE IN THE ABSENCE OF HORIZONTALITY |
CN204058374U (en) * | 2014-08-01 | 2014-12-31 | 中国石油化工股份有限公司 | Fluid prearranged assignment device and fluid prearranged assignment dish |
CN204841616U (en) * | 2015-08-04 | 2015-12-09 | 中石化炼化工程(集团)股份有限公司 | Bushing type gas -liquid distributor |
CN204952859U (en) * | 2015-08-31 | 2016-01-13 | 中国石化工程建设有限公司 | Gas -liquid distributor |
-
2017
- 2017-11-24 TW TW106140943A patent/TWI664021B/en active
- 2017-11-24 RU RU2017140962A patent/RU2672742C1/en active
- 2017-11-24 GB GB1719542.1A patent/GB2560066B/en active Active
- 2017-11-24 KR KR1020170158615A patent/KR101989328B1/en active IP Right Grant
- 2017-11-24 SG SG10201709746QA patent/SG10201709746QA/en unknown
Also Published As
Publication number | Publication date |
---|---|
GB2560066B (en) | 2020-07-29 |
GB2560066A (en) | 2018-08-29 |
KR20180059374A (en) | 2018-06-04 |
RU2672742C1 (en) | 2018-11-19 |
TW201825171A (en) | 2018-07-16 |
KR101989328B1 (en) | 2019-06-14 |
GB201719542D0 (en) | 2018-01-10 |
TWI664021B (en) | 2019-07-01 |
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