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US4521139A
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Method of regulating mass streams
Assignee: Brennstoffinstitut Freiberg
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Filing: 1982-07-19
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Granted: 1985-06-04
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Expires: 2002-07-19
Abstract
Abstract A method of adjusting the mass stream and flow density of a finely divided, fine-grained solid fuel is described. The method uses a dosing container having a fluidized bed at its bottom part and into which the solid fuel is charged above the fluidized bed. A fluidizing gas is adjustably fed to the bottom part of the container and a compensation gas is fed to the upper part of the latter. Mass stream parameters and density are measured in the discharge or supply pipe communicating with the fluidizing bed and the required weight of flow of the fluidizing gas is computed by a computer. In this manner, the regulation of the mass stream is effected by adjusting the loose density of the charge of the dusty material in the container.
Inventors
- 👤 Horst Kretschmer
- 👤 Guenter Tietze
- 👤 Juergen Noack
- 👤 Hans-Joachim Schweigel
- 👤 Manfred Schingnitz
- 👤 Klaus Werner
- 👤 Bernd Kirsch
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 21:50
CPC Classifications
C; C10; C10J; C10J3/00; C10J3/72; C10J3/723; B; B65; B65G; B65G53/00; B65G53/34; B65G53/66; C10J3/46; C10J3/48; C10J3/485; C21; C21B; C21B5/00; C21B5/001; C21B5/003; F; F23; F23N; F23N5/00; F23N5/18; C10J2300/00; C10J2300/12; C10J2300/1223; F23N2221/00; F23N2221/10; F23N2237/00; F23N2237/18; F23N2239/00; F23N2239/02
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
198 words
A method of regulating a continuous mass stream of a finely divided, fine-grained solid fuel which is conveyed pneumatically at an arbitrary concentration and pressure from a closed dosing container through a supply pipe to a gasification reactor or a burner of a heater or steam boiler, comprising the steps of charging the solid fuel into the closed dosing container to create therein a charge of a bulk density ρ S ; forming a fluidized bed in the charge near the bottom part of the container by means of supplying a fluidizing gas V G ; feeding a compensation gas V KG into a part of the container which is remote from the fluidizd bed; discharging a mass stream of the solid fuel with a mass stream rate m K from the fluidized bed through the supply pipe; maintaining the flow density ρ f1 of the mass stream in the supply pipe at a costant required value by regulation the fluidizing gas V G depending upon the required flow density ρ f1 ; and regulating of the mass stream rate m K in the supply pipe by adjusting the compensation gas V KG according to the equation ##EQU3##
Claim 2
Independent Claim
198 words
A method of regulating a continuous mass stream of a finely divided, fine-grained solid fuel which is conveyed pneumatically at an arbitrary concentration and pressure from a closed dosing container through a supply pipe to a gasification reactor or a burner of a heater or steam boiler, comprising the steps of charging the solid fuel into the closed dosing container to create therein a charge of a bulk density ρ S ; forming a fluidized bed in the charge near the bottom part of the container by means of supplying a fluidizing gas V G ; feeding a compensation gas V KG into a part of the container which is remote from the fluidizd bed; discharging a mass stream of the solid fuel with a mass stream rate m K from the fluidized bed through the supply pipe; maintaining the flow density ρ f1 of the mass stream in the supply pipe at a costant required value by regulation the fluidizing gas V G depending upon the required flow density ρ f1 ; and regulating of the mass stream rate m K in the supply pipe by adjusting the compensation gas V KG according to the equation ##EQU3##
Claim 3
Dependent Claim
80 words
A method as defined in claim 1, wherein the flow density ρ f1 of the mass stream in the supply pipe is maintained at a constant required value by regulation of the fluidizing gas V G depending upon the required flow density ρ f1 according to the equation ##EQU4## ρ G being the density of the gas in the said container measured at the pressure and the temperature conditions therein, and ρ K the grain density of the solid fuel.
Claim 4
Dependent Claim
50 words
A method as defined in claim 1, wherein the desired flow density ρ f1 in the supply pipe is continuously sensed by a flow density measuring probe and the flow of the fluidizing gas is continuously regulated so as to compensate for any density fluctuations by varying the mass stream.
Claim 5
Dependent Claim
101 words
A method as defined in claim 1, further comprising the steps of maintaining a constant difference pressure between the container and the gasification reactor or burner so as to get a required maximum mass stream rate m K ; mixing the mass stream at a mixing point in the supply pipe with a control gas stream V SG being fed to the supply pipe; adjusting a required mass stream rate m K below the said maximum mass stream rate by varying the control gas stream V SG inverse proportionally to the desired varying of the mass stream rate m K .
Claim 6
Dependent Claim
68 words
A method as defined in claim 4, wherein a plurality of n supply pipe communicates with the region of the fluidized bed in the container, and wherein the mass stream in at least one supply pipe i of the supply pipe n is mixed with a control gas stream V SG which is being fed to the supply pipe i with a mass stream rate m Ki .
Claim 7
Dependent Claim
41 words
A method as defined in claim 5, wherein the compensation gas V KG is adjusted according to the equation ##EQU5## wherein m K is the (total) mass stream rate, defined as the sum of mass streams through all supply pipes n.
Claim 8
Independent Claim
104 words
A method as defined in claims 2 or 5, wherein the required flow density ρ f1 of the mass streams in the supply pipes upstream of the mixing point is maintained at a constant value which is higher than an allowable minimum flow density, by regulation of the fluidizing gas V G , the latter depending upon the required flow density ρ f1 according to the equation ##EQU6## wherein m K is the (total) mass stream rate, defined by the equation ##EQU7## as the sum of the mass stream rates n Ki of the supply pipes i of the said plurality of supply pipes.
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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) | 1988-06-03 | 1988-12-03 | 1989-06-04 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-06-03 | 1992-12-03 | 1993-06-04 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-06-03 | 1996-12-03 | 1997-06-04 | $7700.00 | Window Closed / Lapsed |