US4169714A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Removal of fine particles from a gas stream by solid particle addition in venturi contactor
Assignee: SAN DIEGO TRUST & SAVINGS BANK
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Filing: 1977-01-14
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Granted: 1979-10-02
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Expires: 1997-01-14
Abstract
Abstract Fine particles contaminating a gas stream are removed from the gas stream by moving the gas stream at a velocity of between 50 and 500 feet per second; dispersing relatively larger solid collector particles in the gas stream to cause the collector particles to capture the fine particles by interception and inertial impaction and thereby form agglomerates consisting of the collector particles having the fine particles adhered thereto; and removing the agglomerates from the gas stream. Following removal from the gas stream the agglomerates may be cleaned to separate the fine particle material from the collector particles so that the collector particles can be redispersed into the gas stream.
Inventors
- 👤 Seymour Calvert
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 19:16
CPC Classifications
B; B01; B01D; B01D51/00; B01D51/02; B01D51/04; B03; B03C; B03C3/00; B03C3/017; B03C3/02; B03C3/04; B03C3/14; B03C3/155; Y; Y10; Y10S; Y10S55/00; Y10S55/25
Claims Analysis
Total Claims: 23
Claim 1
Independent Claim
238 words
A process for removing finely divided solid particulate matter at high efficiency from a gas stream by interception and inertial impaction, comprising: (a) moving a gas stream containing finely divided solid or liquid particulate matter at a velocity of between 100 and 300 feet per second in a given direction through a tubular venturi contactor; (b) dispersing relatively larger solid collector particles into said gas stream at a negligible velocity in said given direction as said gas stream flows through said tubular venturi contactor, said collector particles being sufficiently large so as to cause said collector particles to capture said particulate matter by interception and inertial impaction and thereby form agglomerates consisting of said collector particles having said particulate matter adhered thereto, the amount of collector particles being dispersed selected such that the ratio of the flow rate of the collector particles to the flow rate of the gas is at least (0.001 gm/sec)/(cm 3 /sec); (c) maintaining the pressure drop across said tubular contactor to at least 9.3 cm water column; wherein said velocity of the gas stream, size of the collector particles, and ratio of flow rate of collector particles to flow rate of gas is further selected from the limitations set forth in (a), (b) and (c) above such that approximately 99% of the particulate matter in the gas stream is captured by said collector particles; and (d) removing said agglomerates from said gas stream.
Claim 2
Dependent Claim
238 words
A process for removing finely divided solid particulate matter at high efficiency from a gas stream by interception and inertial impaction, comprising: (a) moving a gas stream containing finely divided solid or liquid particulate matter at a velocity of between 100 and 300 feet per second in a given direction through a tubular venturi contactor; (b) dispersing relatively larger solid collector particles into said gas stream at a negligible velocity in said given direction as said gas stream flows through said tubular venturi contactor, said collector particles being sufficiently large so as to cause said collector particles to capture said particulate matter by interception and inertial impaction and thereby form agglomerates consisting of said collector particles having said particulate matter adhered thereto, the amount of collector particles being dispersed selected such that the ratio of the flow rate of the collector particles to the flow rate of the gas is at least (0.001 gm/sec)/(cm 3 /sec); (c) maintaining the pressure drop across said tubular contactor to at least 9.3 cm water column; wherein said velocity of the gas stream, size of the collector particles, and ratio of flow rate of collector particles to flow rate of gas is further selected from the limitations set forth in (a), (b) and (c) above such that approximately 99% of the particulate matter in the gas stream is captured by said collector particles; and (d) removing said agglomerates from said gas stream.
Claim 3
Dependent Claim
35 words
A process according to claim 1, wherein said dispersing step comprises dispersing said collector particles into a pressurized second gas stream; and pumping said pressurized second gas stream into said gas stream containing fine particles.
Claim 4
Dependent Claim
21 words
A process according to claim 1, wherein said collector particles are dispersed into said gas stream by the force of gravity.
Claim 5
Dependent Claim
43 words
A process according to claim 1, further comprising cleaning said agglomerates to separate said fine particle material from said collector particles following removal of said agglomerates from said gas stream; and redispersing said separated collector particles into said gas stream containing fine particles.
Claim 6
Dependent Claim
30 words
A process according to claim 4, wherein the cleaning step comprises detaching said fine particles from said collector particles; and elutriating said detached fine particles away from said collector particles.
Claim 7
Dependent Claim
33 words
A process according to claim 1, further comprising; electrostatically charging said fine particles and said collector particles to opposite polarities to provide an electrostatic attraction between said fine particles and said collector particles.
Claim 8
Dependent Claim
26 words
A process according to claim 1, further comprising; electrostatically charging said fine particles to provide an electrostatic attraction between said fine particles and said collector particles.
Claim 9
Dependent Claim
26 words
A process according to claim 1, further comprising; electrostatically charging said collector particles to provide an electrostatic attraction between said fine particles and said collector particles.
Claim 10
Dependent Claim
28 words
A process according to claim 1 wherein the aerodynamic diameter of said collector particles is at least ten times larger than that of said finely divided particulate matter.
Claim 11
Dependent Claim
31 words
A process according to claim 1 wherein the ratio of the flow rate of the collector particles to the flow rate of the gas is at least (0.002 gm/sec)/(cm 3 /sec).
Claim 12
Dependent Claim
27 words
A process according to claim 1 wherein the median diameter of the finely divided particulate matter is 38 μmA with a geometric standard deviation of approximately 5.
Claim 13
Dependent Claim
230 words
A process for removing finely divided solid particulate matter at high efficiency from a gas stream by interception and inertial impaction, comprising: (a) dispersing relatively larger solid collector particles into said gas stream as said gas stream flows through a tubular venturi contactor containing finely divided solid particulate matter; (b) moving said gas stream having said collector particles dispersed therein at a velocity of between 100 and 300 feet per second through said tubular venturi contactor, said collector particles being sufficiently large so as to cause said collector particles to capture said particulate matter by interception and inertial impaction and thereby form agglomerates consisting of said collector particles having said particulate matter adhered thereto, the amount of collector particles being dispersed selected such that the ratio of the flow rate of the collector particles to the flow rate of the gas is at least (0.001 gm/sec)/(cm 3 /sec); (c) maintaining the pressure drop across said tubular contactor to at least 9.3 cm water column; wherein said velocity of the gas stream, size of the collector particles, and ratio of flow rate of collector particles to flow rate of gas is further selected from the limitations set forth in (a), (b) and (c) above such that approximately 99% of the particulate matter in the gas stream is captured by said collector particles; and (d) removing said agglomerates from said gas stream.
Claim 14
Dependent Claim
230 words
A process for removing finely divided solid particulate matter at high efficiency from a gas stream by interception and inertial impaction, comprising: (a) dispersing relatively larger solid collector particles into said gas stream as said gas stream flows through a tubular venturi contactor containing finely divided solid particulate matter; (b) moving said gas stream having said collector particles dispersed therein at a velocity of between 100 and 300 feet per second through said tubular venturi contactor, said collector particles being sufficiently large so as to cause said collector particles to capture said particulate matter by interception and inertial impaction and thereby form agglomerates consisting of said collector particles having said particulate matter adhered thereto, the amount of collector particles being dispersed selected such that the ratio of the flow rate of the collector particles to the flow rate of the gas is at least (0.001 gm/sec)/(cm 3 /sec); (c) maintaining the pressure drop across said tubular contactor to at least 9.3 cm water column; wherein said velocity of the gas stream, size of the collector particles, and ratio of flow rate of collector particles to flow rate of gas is further selected from the limitations set forth in (a), (b) and (c) above such that approximately 99% of the particulate matter in the gas stream is captured by said collector particles; and (d) removing said agglomerates from said gas stream.
Claim 15
Dependent Claim
30 words
A process according to claim 11, wherein the cleaning step comprises detaching said fine particles from said collector particles; and elutriating said detached fine particles away from said collector particles.
Claim 16
Dependent Claim
33 words
A process according to claim 12, further comprising; electrostatically charging said fine particles and said collector particles to opposite polarities to provide an electrostatic attraction between said fine particles and said collector particles.
Claim 17
Dependent Claim
26 words
A process according to claim 12, further comprising; electrostatically charging said fine particles to provide an electrostatic attraction between said fine particles and said collector particles.
Claim 18
Dependent Claim
26 words
A process according to claim 12, further comprising; electrostatically charging said collector particles to provide an electrostatic attraction between said fine particles and said collector particles.
Claim 19
Dependent Claim
31 words
A process according to claim 12 wherein the ratio of the flow rate of the collector particles to the flow rate of the gas is at least (0.002 gm/sec)/cm 3 /sec).
Claim 20
Dependent Claim
40 words
A process according to claim 7, further comprising cleaning said agglomerates to separate said fine particle material from said collector particles following removal of said agglomerates from said gas stream; and redispersing said separated collector particles into said gas stream.
Claim 21
Dependent Claim
35 words
A process according to claim 7, wherein said dispersing step comprises dispersing said collector particles into a second pressurized gas stream; and pumping said pressurized second gas stream into said gas stream containing fine particles.
Claim 22
Dependent Claim
26 words
A process according to claim 7, wherein said collector particles are dispersed into said gas stream prior to said gas stream being moved at said velocity.
Claim 23
Dependent Claim
24 words
A process according to claim 9, wherein the dispersing step includes dispersing said collector particles into said gas stream by the force of gravity.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1982-10-01 | 1983-04-02 | 1983-10-02 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-10-01 | 1987-04-02 | 1987-10-02 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-10-01 | 1991-04-02 | 1991-10-02 | $7700.00 | Window Closed / Lapsed |