US4684296A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method and apparatus for the generation and utilization of a spiral gas stream in a pipeline
Assignee: Individual
•
Filing: 1986-10-24
•
Granted: 1987-08-04
•
Expires: 2006-10-24
Abstract
Abstract Uniform flow of gas flowing in a cylinder having inner diameter larger than that of a pipeline is introduced through a funnelform reducer into the inlet of the pipeline, where uniform flow of gas turned to a spiral gas stream by bringing to the mean gas stream velocity faster than 20 meter per second there. When solid particles are introduced into the spiral gas strem zone, they are transported to the outlet of the pipeline. A compressed gas layer is formed along the inside wall of the pipeline by the spiral motion of gas stream, and the layer prevents the direct contact of the solid particles to the inside wall of the pipeline which causes the erosion of the pipeline. As the center part of the cross section of the pipeline becomes very low pressure, especially along the axis of the pipeline, solid particles containing or accompanying volatile matters are desiccated or concentrated as a result of the evaporation of volatile matters while being transported in the pipeline. When grinding powder (abrasive) is transported by the spiral gas stream and spattered on an object, the surface of the object is ground without consumption of much energy.
Inventors
- 👤 Kiyoshi Horii
- 👤 Toshiaki Murata
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 21:45
CPC Classifications
B; B65; B65G; B65G53/00; B65G53/34; B65G53/40; B65G53/42; B65G53/48; Y; Y10; Y10T; Y10T137/00; Y10T137/0318; Y10T137/206; Y10T137/2087
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
166 words
A method for generation of a spiral gas stream in a pipeline which comprises the following steps: forming a uniform flow of gas in a cylinder with first and second ends, the first end adapted for connecting to a pipeline pipe, said second end being closed with a bottom plate and said cylinder having an inner diameter larger than that of said pipeline pipe, by introducing feed gas into said cylinder through a gas inlet pipe so as to make the flow line of the feed gas substantially intersect the longitudinal axis of the cylinder; bringing the mean gas flow velocity in said cylinder to a mean gas flow velocity less than 10 meters per second; introducing said uniform flow of gas flowing in said cylinder into the inlet of said pipeline pipe through a funnelform reducer connected at said first end of said cylinder; and bringing the mean gas stream velocity in the pipeline pipe to a mean velocity greater than 20 meters per second.
Claim 2
Independent Claim
166 words
A method for generation of a spiral gas stream in a pipeline which comprises the following steps: forming a uniform flow of gas in a cylinder with first and second ends, the first end adapted for connecting to a pipeline pipe, said second end being closed with a bottom plate and said cylinder having an inner diameter larger than that of said pipeline pipe, by introducing feed gas into said cylinder through a gas inlet pipe so as to make the flow line of the feed gas substantially intersect the longitudinal axis of the cylinder; bringing the mean gas flow velocity in said cylinder to a mean gas flow velocity less than 10 meters per second; introducing said uniform flow of gas flowing in said cylinder into the inlet of said pipeline pipe through a funnelform reducer connected at said first end of said cylinder; and bringing the mean gas stream velocity in the pipeline pipe to a mean velocity greater than 20 meters per second.
Claim 3
Independent Claim
186 words
A method for the transportation of solid particles through a pipeline which comprises the following steps: forming a uniform flow of gas in a cylinder with first and second ends, the first end adapted for connecting to a pipeline pipe, said second end being closed with a bottom plate and said cylinder having an inner diameter larger than that of the pipeline pipe, by introducing feed gas into said cylinder through a gas inlet pipe so as to make the flow line of the feed gas substantially intersect the longitudinal axis of the cylinder; bringing the mean gas flow velocity in said cylinder to a mean gas flow velocity less than 10 meters per second; generating a spiral gas stream in said pipeline pipe by introducing said uniform flow of gas flowing in said cylinder into the inlet of said pipeline pipe through a funnelform reducer connected at said first end of said cylinder; bringing the mean gas stream velocity in said pipeline pipe to a mean velocity greater than 20 meters per second; and feeding solid particles into said spiral gas stream zone thus generated.
Claim 4
Independent Claim
186 words
A method for the transportation of solid particles through a pipeline which comprises the following steps: forming a uniform flow of gas in a cylinder with first and second ends, the first end adapted for connecting to a pipeline pipe, said second end being closed with a bottom plate and said cylinder having an inner diameter larger than that of the pipeline pipe, by introducing feed gas into said cylinder through a gas inlet pipe so as to make the flow line of the feed gas substantially intersect the longitudinal axis of the cylinder; bringing the mean gas flow velocity in said cylinder to a mean gas flow velocity less than 10 meters per second; generating a spiral gas stream in said pipeline pipe by introducing said uniform flow of gas flowing in said cylinder into the inlet of said pipeline pipe through a funnelform reducer connected at said first end of said cylinder; bringing the mean gas stream velocity in said pipeline pipe to a mean velocity greater than 20 meters per second; and feeding solid particles into said spiral gas stream zone thus generated.
Claim 5
Dependent Claim
23 words
A method according to claim 2 wherein said solid particles are a mixture of larger size solid particles and smaller size solid particles.
Claim 6
Dependent Claim
23 words
A method according to claim 2 wherein said solid particles are a mixture of heavier weight solid particles and lighter weight solid particles.
Claim 7
Independent Claim
194 words
A method for the desiccation or concentration of solid particles containing or accompanying volatile matter which comprises the following steps: forming a uniform flow of gas in a cylinder with first and second ends, the first end adapted for connecting to a pipeline pipe, said second end being closed with a bottom plate and said cylinder having an inner diameter larger than that of the pipeline pipe, by introducing feed gas into the cylinder through a gas inlet pipe so as to make the flow line of the feed gas substantially intersect the longitudinal axis of said cylinder; bringing the mean gas flow velocity in said cylinder to a mean gas flow velocity less than 10 meters per second; generating a spiral gas stream in said pipeline pipe by introducing said uniform flow of gas flowing in said cylinder into the inlet of said pipeline pipe through a funnelform reducer connected at said first end of said cylinder; bringing the mean gas stream velocity in said pipeline to a mean velocity greater than 20 meters per second; and feeding solid particles containing or accompanying volatile matter into said spiral gas stream zone thus generated.
Claim 8
Independent Claim
194 words
A method for the desiccation or concentration of solid particles containing or accompanying volatile matter which comprises the following steps: forming a uniform flow of gas in a cylinder with first and second ends, the first end adapted for connecting to a pipeline pipe, said second end being closed with a bottom plate and said cylinder having an inner diameter larger than that of the pipeline pipe, by introducing feed gas into the cylinder through a gas inlet pipe so as to make the flow line of the feed gas substantially intersect the longitudinal axis of said cylinder; bringing the mean gas flow velocity in said cylinder to a mean gas flow velocity less than 10 meters per second; generating a spiral gas stream in said pipeline pipe by introducing said uniform flow of gas flowing in said cylinder into the inlet of said pipeline pipe through a funnelform reducer connected at said first end of said cylinder; bringing the mean gas stream velocity in said pipeline to a mean velocity greater than 20 meters per second; and feeding solid particles containing or accompanying volatile matter into said spiral gas stream zone thus generated.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1990-08-03 | 1991-02-02 | 1991-08-04 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-08-03 | 1995-02-02 | 1995-08-04 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-08-03 | 1999-02-02 | 1999-08-04 | $7700.00 | Window Closed / Lapsed |