RU97113062A - TWO COMPONENT LIQUID SPRAY NOZZLE - Google Patents
TWO COMPONENT LIQUID SPRAY NOZZLEInfo
- Publication number
- RU97113062A RU97113062A RU97113062/25A RU97113062A RU97113062A RU 97113062 A RU97113062 A RU 97113062A RU 97113062/25 A RU97113062/25 A RU 97113062/25A RU 97113062 A RU97113062 A RU 97113062A RU 97113062 A RU97113062 A RU 97113062A
- Authority
- RU
- Russia
- Prior art keywords
- liquid
- outlet
- gas
- mixing chamber
- fluidized bed
- Prior art date
Links
- 239000007788 liquid Substances 0.000 title claims 14
- 239000007921 spray Substances 0.000 title 1
- 239000012530 fluid Substances 0.000 claims 3
- 239000000203 mixture Substances 0.000 claims 3
- 230000035515 penetration Effects 0.000 claims 2
Claims (9)
y=a+bF(x),
где
а и b являются постоянными величинами, равными а=507,469, b=5400,409;
и
и (II) перепад давления в смесительной камере составляет 0,8-1,5 бар.1. A method of injecting liquid directly into the fluidized bed, which involves the use of nozzles or nozzles, each of which has (a) at least one inlet for pressurized liquid, (b) at least one inlet for atomizing gas, (c) a mixing chamber for mixing liquid and gas, and (d) at least one outlet through which a mixture of gas and liquid is supplied from the mixing chamber directly into the fluidized bed, characterized in that (I) the penetration depth the fluid leaving from each outlet in the fluidized bed in the horizontal direction is 250-2500 mm and is determined from the equation:
y = a + bF (x),
Where
a and b are constant values equal to a = 507.469, b = 5400.409;
and
and (II) the pressure drop in the mixing chamber is 0.8-1.5 bar.
и (II) перепад давления в смесительной камере составляет 0,8-1,5 бар.4. A method of injecting liquid directly into the fluidized bed, which involves the use of nozzles or nozzles, each of which has (a) at least one inlet for pressurized liquid, (b) at least one inlet for atomizing gas, (c) a mixing chamber for mixing liquid and gas, and (d) at least one outlet through which a mixture of gas and liquid is supplied from the mixing chamber directly into the fluidized bed, characterized in that (I) the flow rate (R) of the liquid through each outlet is 0.009-0.130 m 3 / h / mm 2 and is determined from the equation:
and (II) the pressure drop in the mixing chamber is 0.8-1.5 bar.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GBGB9500226.7A GB9500226D0 (en) | 1995-01-06 | 1995-01-06 | Nozzle |
GB9500226.7 | 1995-01-06 |
Publications (2)
Publication Number | Publication Date |
---|---|
RU97113062A true RU97113062A (en) | 1999-06-27 |
RU2156663C2 RU2156663C2 (en) | 2000-09-27 |
Family
ID=10767679
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
RU97113062/12A RU2156663C2 (en) | 1995-01-06 | 1995-12-21 | Two-component injector for liquid spraying |
Country Status (28)
Country | Link |
---|---|
US (1) | US6088934A (en) |
EP (1) | EP0801591B1 (en) |
JP (1) | JPH10511890A (en) |
KR (1) | KR100419325B1 (en) |
CN (1) | CN1177309A (en) |
AT (1) | ATE179906T1 (en) |
AU (1) | AU699258B2 (en) |
BG (1) | BG62958B1 (en) |
BR (1) | BR9510131A (en) |
CA (1) | CA2209292A1 (en) |
CZ (1) | CZ208097A3 (en) |
DE (1) | DE69509679T2 (en) |
DZ (1) | DZ1960A1 (en) |
ES (1) | ES2131349T3 (en) |
FI (1) | FI972866A0 (en) |
GB (1) | GB9500226D0 (en) |
GR (1) | GR3030922T3 (en) |
HU (1) | HU221764B1 (en) |
MY (1) | MY113417A (en) |
NO (1) | NO973104D0 (en) |
NZ (1) | NZ297536A (en) |
PL (1) | PL321255A1 (en) |
RU (1) | RU2156663C2 (en) |
SK (1) | SK282170B6 (en) |
TW (1) | TW329397B (en) |
UA (1) | UA39989C2 (en) |
WO (1) | WO1996020780A1 (en) |
ZA (1) | ZA9634B (en) |
Families Citing this family (26)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0853091A1 (en) * | 1997-01-13 | 1998-07-15 | Bp Chemicals S.N.C. | Polymerisation process |
US6075101A (en) * | 1997-02-19 | 2000-06-13 | Union Carbide Chemicals & Plastics Technology Corporation | Control of solution catalyst droplet size with a perpendicular spray nozzle |
US5962606A (en) * | 1997-02-19 | 1999-10-05 | Union Carbide Chemicals & Plastics Technology Corporation | Control of solution catalyst droplet size with an effervescent spray nozzle |
US6306981B1 (en) | 1999-04-02 | 2001-10-23 | Union Carbide Chemicals & Plastics Technology Corporation | Gas phase polymerization process |
FR2792853B1 (en) | 1999-04-30 | 2001-07-06 | Bp Chemicals Snc | SPRING NOZZLE WITH 360 DEGREE SLOT, FOR LIQUID INJECTION INTO A FLUIDIZED BED REACTOR |
BR9905840B1 (en) * | 1999-12-14 | 2010-07-13 | load dispersing system of fluid catalytic cracking units. | |
FR2806327B1 (en) | 2000-03-17 | 2002-06-14 | Bp Chemicals Snc | VARIABLE LIQUID LEVEL NOZZLE |
DE10317533A1 (en) * | 2003-04-16 | 2004-11-04 | Basell Polyolefine Gmbh | Metering, e.g. catalyst into reactor containing fluidized particles bed in partly gaseous medium by introducing fluid stream into reactor so that region with reduced particle density is formed in fluidized bed around metering point(s) |
EP1491253A1 (en) * | 2003-06-26 | 2004-12-29 | Urea Casale S.A. | Fluid bed granulation process and apparatus |
ES2421887T3 (en) * | 2007-03-30 | 2013-09-06 | Univation Tech Llc | Systems and methods for manufacturing polyolefins |
BRPI0905782A2 (en) * | 2008-01-24 | 2015-07-14 | Dow Global Technologies Inc | Catalyst injection nozzle, method for producing a polymer in a gas phase polymerization reactor and substantially friable polymer composition |
WO2009114571A2 (en) * | 2008-03-11 | 2009-09-17 | Selas Fluid Processing Corporation | System and method for flameless thermal oxidation at optimized equivalence ratios |
US9970683B2 (en) | 2008-03-11 | 2018-05-15 | Linde Engineering North America Inc. | Apparatus and method for flameless thermal oxidation at optimized equivalence ratios |
EP2172262A1 (en) * | 2008-10-03 | 2010-04-07 | Ineos Europe Limited | Process |
US8841391B2 (en) | 2008-10-03 | 2014-09-23 | Ineos Sales (Uk) Limited | Process for the introduction of a polymerisation catalyst into a gas-phase fluidised bed |
JP2012520759A (en) * | 2009-03-20 | 2012-09-10 | スソンテック カンパニー リミテッド | Thermal conversion reaction sealed container |
RU2411758C1 (en) * | 2009-10-19 | 2011-02-20 | Михаил Валерьевич Корин | Popcorn preparation apparatus |
WO2013112170A1 (en) * | 2012-01-27 | 2013-08-01 | International Engine Intellectual Property Company, Llc | Cross style (4 port) ammonia gas injector |
US9551255B2 (en) * | 2012-04-13 | 2017-01-24 | International Engine Intellectual Property Company, Llc | Mixing plate as stabilizer for ammonia gas injector |
RU2548703C1 (en) * | 2014-04-23 | 2015-04-20 | Владислав Юрьевич Климов | Nozzle of steam-gas generator mixing head |
US9950328B2 (en) * | 2016-03-23 | 2018-04-24 | Alfa Laval Corporate Ab | Apparatus for dispersing particles in a fluid |
US10857507B2 (en) * | 2016-03-23 | 2020-12-08 | Alfa Laval Corporate Ab | Apparatus for dispersing particles in a liquid |
US10272385B2 (en) | 2016-05-17 | 2019-04-30 | Linde Engineering North America, Inc. | Flameless thermal oxidizer for oxidizing gaseous effluent streams containing hydrogen gas |
CN109855090B (en) * | 2019-01-21 | 2020-08-04 | 昆明理工大学 | Efficient biomass liquid fuel atomizing and burning system and method |
WO2020153959A1 (en) * | 2019-01-24 | 2020-07-30 | Lummus Novolen Technology Gmbh | Centric spray pipe |
US11958105B2 (en) | 2022-03-09 | 2024-04-16 | Honda Motor Co., Ltd. | Rapid solidification of molded products |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SE426097B (en) * | 1978-12-05 | 1982-12-06 | Stal Laval Turbin Ab | COMBINED AIR AND FUEL NOZZLE FOR SPEED BED STOVES |
JPS58182006A (en) * | 1982-04-20 | 1983-10-24 | Ishikawajima Harima Heavy Ind Co Ltd | Fluidized bed combustion system |
ZA844157B (en) | 1983-06-06 | 1986-01-29 | Exxon Research Engineering Co | Process and catalyst for polyolefin density and molecular weight control |
CA1268754A (en) | 1985-06-21 | 1990-05-08 | Howard Curtis Welborn, Jr. | Supported polymerization catalyst |
US5055438A (en) | 1989-09-13 | 1991-10-08 | Exxon Chemical Patents, Inc. | Olefin polymerization catalysts |
NZ235032A (en) | 1989-08-31 | 1993-04-28 | Dow Chemical Co | Constrained geometry complexes of titanium, zirconium or hafnium comprising a substituted cyclopentadiene ligand; use as olefin polymerisation catalyst component |
SE465502B (en) * | 1990-02-12 | 1991-09-23 | Johansson Sven Halvor | NOZZLE DEVICE FOR EXHAUSTING A GAS / HYDROGEN MIXTURE INTO A PROCESS GAS |
ZA943399B (en) * | 1993-05-20 | 1995-11-17 | Bp Chem Int Ltd | Polymerisation process |
-
1995
- 1995-01-06 GB GBGB9500226.7A patent/GB9500226D0/en active Pending
- 1995-12-21 KR KR1019970704624A patent/KR100419325B1/en not_active IP Right Cessation
- 1995-12-21 CN CN95197754A patent/CN1177309A/en active Pending
- 1995-12-21 UA UA97084120A patent/UA39989C2/en unknown
- 1995-12-21 RU RU97113062/12A patent/RU2156663C2/en not_active IP Right Cessation
- 1995-12-21 NZ NZ297536A patent/NZ297536A/en unknown
- 1995-12-21 HU HU9702093A patent/HU221764B1/en not_active IP Right Cessation
- 1995-12-21 EP EP95941228A patent/EP0801591B1/en not_active Expired - Lifetime
- 1995-12-21 BR BR9510131A patent/BR9510131A/en not_active Application Discontinuation
- 1995-12-21 PL PL95321255A patent/PL321255A1/en unknown
- 1995-12-21 DE DE69509679T patent/DE69509679T2/en not_active Expired - Fee Related
- 1995-12-21 AU AU42706/96A patent/AU699258B2/en not_active Ceased
- 1995-12-21 JP JP8520798A patent/JPH10511890A/en active Pending
- 1995-12-21 CZ CZ972080A patent/CZ208097A3/en unknown
- 1995-12-21 WO PCT/GB1995/003007 patent/WO1996020780A1/en active IP Right Grant
- 1995-12-21 ES ES95941228T patent/ES2131349T3/en not_active Expired - Lifetime
- 1995-12-21 SK SK908-97A patent/SK282170B6/en unknown
- 1995-12-21 CA CA002209292A patent/CA2209292A1/en not_active Abandoned
- 1995-12-21 AT AT95941228T patent/ATE179906T1/en not_active IP Right Cessation
- 1995-12-28 TW TW084114054A patent/TW329397B/en not_active IP Right Cessation
-
1996
- 1996-01-03 DZ DZ960001A patent/DZ1960A1/en active
- 1996-01-03 ZA ZA9634A patent/ZA9634B/en unknown
- 1996-01-04 MY MYPI96000028A patent/MY113417A/en unknown
-
1997
- 1997-06-25 BG BG101667A patent/BG62958B1/en unknown
- 1997-07-03 US US08/888,052 patent/US6088934A/en not_active Expired - Fee Related
- 1997-07-03 NO NO973104A patent/NO973104D0/en unknown
- 1997-07-04 FI FI972866A patent/FI972866A0/en not_active Application Discontinuation
-
1999
- 1999-08-04 GR GR990402006T patent/GR3030922T3/en unknown
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