Method of regulating mass streams

• US 4,521,139 A
• Filed: 07/19/1982
• Issued: 06/04/1985
• Est. Priority Date: 07/17/1981
• Status: Expired due to Fees

• Current Assignee: Brennstoffinstitut Freiberg
• Original Assignee: Brennstoffinstitut Freiberg
• Inventors: Schingnitz, Manfred, Kretschmer, Horst, Werner, Klaus, Noack, Juergen, Tietze, Guenter, Kirsch, Bernd, Schweigel, Hans-Joachim
• Primary Examiner(s): Nase, Jeffrey V.
• Assistant Examiner(s): Williams, L. E.
• Application Number:
  US06/399,989
• Time in Patent Office: 1,051 Days
• Field of Search: 406/138, 406/141, 406/142, 406/143, 406/144, 406/197, 406/12, 406/14, 406/19, 406/10
• US Class Current: 406/19
• CPC Class Codes: B65G 53/66 Use of indicator or control devices, e.g. for controlling gas pressure, for controlling proportions of material and gas, for indicating or preventing jamming of material controlling the flow of coal firing systems C21B5/003
• CPC Class Codes: C10J 2300/1223 by burners
• CPC Class Codes: C10J 3/485 Entrained flow gasifiers
• CPC Class Codes: C10J 3/723 Controlling or regulating the gasification process
• CPC Class Codes: C21B 5/003 Injection of pulverulent coal
• CPC Class Codes: F23N 2221/10 Analysing fuel properties, e.g. density, calorific
• CPC Class Codes: F23N 2237/18 fluidized bed burners
• CPC Class Codes: F23N 2239/02 Solid fuels
• CPC Class Codes: F23N 5/18 using detectors sensitive to rate of flow of air or fuel

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.

Claims

1. 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##

2. 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.

3. 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.

4. 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.

5. 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.

6. 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.

7. 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.