IE42529L - Disengaging particles from gases - Google Patents

Disengaging particles from gases

Info

Publication number
IE42529L
IE42529L IE760619A IE61976A IE42529L IE 42529 L IE42529 L IE 42529L IE 760619 A IE760619 A IE 760619A IE 61976 A IE61976 A IE 61976A IE 42529 L IE42529 L IE 42529L
Authority
IE
Ireland
Prior art keywords
chamber
conduit
cyclones
gas
particles
Prior art date
Application number
IE760619A
Other versions
IE42529B1 (en
Original Assignee
Ashland Oil Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ashland Oil Inc filed Critical Ashland Oil Inc
Publication of IE42529L publication Critical patent/IE42529L/en
Publication of IE42529B1 publication Critical patent/IE42529B1/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C9/00Combinations with other devices, e.g. fans, expansion chambers, diffusors, water locks
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D45/00Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D45/00Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/12Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/005Separating solid material from the gas/liquid stream
    • B01J8/0055Separating solid material from the gas/liquid stream using cyclones
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/24Multiple arrangement thereof

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Cyclones (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Abstract

1533022 Separating particles from gas ASHLAND OIL INC 19 March 1976 [24 March 1975] 11230/76 Headings BIT and B2P An apparatus for separating solid or liquid particles from a gas stream in which they are suspended comprises a chamber 12, a conduit 10 through which the particle-laden gas stream flows, the conduit having an outlet opening 13 leading into the chamber and a side wall port 17 upstream of the opening 13, and a cyclone separator 19 having an inlet connected to the port 17. The apparatus is described in relation to the separation of fine solid catalyst particles from gases produced in catalytic "riser cracking" of petroleum. The conduit 10 is in the form of a riser pipe which enters a gas-disengaging vessel from below and opens at 13 into the disengaging or separating chamber 12. The upper end of the riser pipe is stiffened at 25. As shown, there are two ports 17 in the side wall of the conduit 10 connected to a pair of cyclones 19 which are connected by expansion joints 22 to gas outlet conduits 21 connected to a further pair of cyclones 28 which have gas discharge outlets 30 leading out of the vessel 11 to fractionators. The cyclones 19, 28 have dip legs 20, 29 for discharging separated catalyst particles to the bottom of the vessel 11 from which they are led to a regenerator. The chamber 12 is pressurized by being connected directly to the conduit 10 so that no gas circulation takes place in the chamber. In operation, as the gases are abruptly diverted from the conduit 10 through the ports 17 into the cyclones which are at a lower pressure, the bulk of the catalyst particles are separated from them and are carried by their momentum through the opening 13 into the chamber 12 where they impinge on a deflector 14 which direct them downwardly to the bottom of the chamber. A baffle 33, Fig. 4, may be provided inwardly of the conduit 10 upstream of the port 17 to deflect the particles away from the port. In modifications, the conduit 10 may enter the chamber 12 through its side or top and the cyclones maybe disposed outside of the chamber. Other uses of the apparatus are given. [GB1533022A]
IE619/76A 1975-03-24 1976-03-24 Method and apparatus for disengaging particles from gases IE42529B1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US56162575A 1975-03-24 1975-03-24

Publications (2)

Publication Number Publication Date
IE42529L true IE42529L (en) 1976-11-24
IE42529B1 IE42529B1 (en) 1980-08-27

Family

ID=24242750

Family Applications (1)

Application Number Title Priority Date Filing Date
IE619/76A IE42529B1 (en) 1975-03-24 1976-03-24 Method and apparatus for disengaging particles from gases

Country Status (23)

Country Link
JP (1) JPS51119568A (en)
BE (1) BE839958A (en)
BR (1) BR7601773A (en)
CA (1) CA1043709A (en)
DD (1) DD128137A5 (en)
DE (1) DE2612507B2 (en)
DK (1) DK146032C (en)
ES (1) ES446333A1 (en)
FI (1) FI59536C (en)
FR (1) FR2305219A1 (en)
GB (1) GB1533022A (en)
GR (1) GR59847B (en)
IE (1) IE42529B1 (en)
IL (1) IL49207A (en)
IT (1) IT1058630B (en)
NL (1) NL165950C (en)
NO (1) NO145565C (en)
NZ (1) NZ180266A (en)
PL (1) PL100278B1 (en)
PT (1) PT64939B (en)
SE (1) SE416521B (en)
TR (1) TR19221A (en)
ZA (1) ZA761513B (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4406776A (en) * 1982-08-25 1983-09-27 Uop Inc. Fluidized catalytic cracking process and apparatus
BR8407045A (en) * 1983-09-01 1985-07-30 Noel Carroll PERFECT DISCHARGE OPENING FOR CYCLONIC SEPARATORS
EE05544B1 (en) 2007-09-05 2012-06-15 Aktsiaselts Narva ?Litehas Dust extraction chamber for separating solid particles from a vapor-gas mixture
CN108392929B (en) * 2018-04-24 2023-12-15 中国石油大学(北京) Separation device
CN116037331B (en) * 2023-03-06 2023-06-23 常州长登焊材股份有限公司 Drawing oil circulation system for high-speed winding and drawing machine

Also Published As

Publication number Publication date
FR2305219A1 (en) 1976-10-22
BR7601773A (en) 1976-09-21
GB1533022A (en) 1978-11-22
NZ180266A (en) 1978-07-10
NL7603092A (en) 1976-09-28
FI59536C (en) 1981-09-10
DE2612507B2 (en) 1977-09-08
DK146032C (en) 1983-11-07
IL49207A (en) 1978-09-29
DE2612507A1 (en) 1976-10-14
NO145565B (en) 1982-01-11
FR2305219B1 (en) 1981-02-27
NL165950C (en) 1981-06-15
SE7603606L (en) 1976-09-25
CA1043709A (en) 1978-12-05
PL100278B1 (en) 1978-09-30
ZA761513B (en) 1977-03-30
IE42529B1 (en) 1980-08-27
NL165950B (en) 1981-01-15
PT64939A (en) 1976-04-01
DE2612507C3 (en) 1978-05-11
IT1058630B (en) 1982-05-10
NO145565C (en) 1982-04-21
FI760783A (en) 1976-09-25
GR59847B (en) 1978-03-07
DK126676A (en) 1976-09-25
NO761019L (en) 1976-09-27
ES446333A1 (en) 1977-10-01
PT64939B (en) 1977-08-25
SE416521B (en) 1981-01-19
TR19221A (en) 1978-06-01
IL49207A0 (en) 1976-05-31
DD128137A5 (en) 1977-11-02
JPS51119568A (en) 1976-10-20
FI59536B (en) 1981-05-29
DK146032B (en) 1983-06-06
JPS5437345B2 (en) 1979-11-14
BE839958A (en) 1976-07-16

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