Method and apparatus for injecting wastes into a molten bath with an ejector

• US 5,613,245 A
• Filed: 06/07/1995
• Issued: 03/18/1997
• Est. Priority Date: 06/07/1995
• Status: Expired due to Fees

• Current Assignee: Quantum Catalytics LLC
• Original Assignee: Molten Metal Technology Incorporated
• Inventors: Robert, Edgar J.
• Primary Examiner(s): Drodge, Joseph W.
• Application Number:
  US08/479,507
• Time in Patent Office: 650 Days
• Field of Search: 210/97, 210/143, 210/175, 210/741, 210/774, 210/790, 210/909, 210/90, 110/237, 110/235, 110/346, 110/238, 266/44, 266/82, 266/83, 588/201, 588/205, 588/1, 588/202, 422/62, 422/110, 422/111, 422/112, 422/184.1, 422/232
• US Class Current: 588/314
• CPC Class Codes: A62D 2203/10 Apparatus specially adapted for treating harmful chemical agents; Details thereof
• CPC Class Codes: B01J 10/005 carried out at high temperatures in the presence of a molten material
• CPC Class Codes: B01J 2219/00162 controlling the pressure
• CPC Class Codes: B01J 2219/00164 controlling the flow
• CPC Class Codes: B01J 8/004 by means of a nozzle
• CPC Class Codes: B01J 8/20 with liquid as a fluidising medium
• CPC Class Codes: F27B 3/00 Hearth-type furnaces, e.g. of reverberatory type F27B9/00, F27B11/00, F27B13/00, F27B14/00, F27B15/00, F27B21/00 take precedence; Tank furnaces
• CPC Class Codes: F27D 2003/165 the fluid being a fuel
• CPC Class Codes: F27D 2099/0051 Burning waste as a fuel
• CPC Class Codes: F27D 3/1518 Tapholes
• CPC Class Codes: F27D 3/16 Introducing a fluid jet or current into the charge porous elements for gas flushing of molten metals B22D1/005
• CPC Class Codes: F27D 3/18 Charging particulate material using a fluid carrier
• CPC Class Codes: F27M 2001/05 Waste materials, refuse

Abstract

The present invention relates to a method and an apparatus for injecting a particulate solid into a molten bath. The method includes forming a liquid stream and directing a first portion of the stream through an ejector for subsequent injection into a molten bath. A second portion of the liquid stream is directed into a receiving vessel. A particulate solid is directed into the receiving vessel, wherein the second portion of the liquid stream and the particulate solid combine to form a slurry. The slurry is directed from the receiving vessel to the ejector, whereby the slurry and the first portion of the liquid stream are combined to form a dilute slurry that is injected into the molten bath. The relative flow rates of the first and second liquid streams can be adjusted in direct relation to any change in the ratio of pressure of the two streams, controlling in this way the volume fraction of solids in the diluted slurry.

Claims

1. A method for injecting a particulate solid into a molten bath, comprising the steps of:

a) forming a liquid stream;

b) directing a first portion of said liquid stream through an ejector for subsequent injection into a molten bath;

c) directing an adjustable second portion of the liquid stream into a receiving vessel;

d) directing a particulate solid into said receiving vessel, whereby the second portion of the liquid stream and the particulate solid combine to form a slurry; and

e) directing said slurry from the receiving vessel to the ejector, whereby the slurry and the first portion of the liquid stream are combined to form a dilute slurry that is injected into the molten bath.

2. The method of claim 1, further including the step of adjusting the ratio of flow rate of the second portion of said liquid stream to the flow rate of the first portion in direct relation to a change in the ratio of pressure of the second liquid stream portion to pressure of the first liquid stream portion.

3. The method of claim 2, further including the step of directing a third portion of said liquid stream to a liquid source for said liquid stream.

4. An apparatus for injecting a particulate solid into a molten bath, comprising:

a) an ejector which is in fluid communication with a molten bath;

b) a liquid source in fluid communication with said ejector;

c) means for directing a first portion of a liquid stream from the liquid source through said ejector;

d) a slurry reservoir in fluid communication with said ejector, whereby a slurry in said slurry reservoir can be directed through the ejector and into the molten bath by conduction of said first portion of the liquid stream through said ejector; and

e) means for directing an adjustable second portion of the liquid stream into the slurry reservoir, whereby said second portion of the liquid stream is combined with the slurry in the slurry reservoir.

5. The apparatus of claim 4, further including means for directing particulates into said slurry reservoir.

6. The apparatus of claim 5, further including means for monitoring the ratio of pressure of the first and second portions of the liquid stream.

7. The apparatus of claim 6, further including means for controlling the rate at which the liquid is directed from said first portion of the liquid stream through said ejector.

8. The apparatus of claim 7, further including means for causing change in the ratio of pressure of the first and second portions of the liquid stream to change the rate at which the liquid from said first portion of the liquid stream is directed through the ejector.

9. The apparatus of claim 6, further including means for controlling the rate at which the liquid is directed from said second portion of the liquid stream into said slurry reservoir.

10. The apparatus of claim 9, further including means for causing change in the ratio of pressure of the first and second portions of the liquid stream to change the rate at which the second portion of the liquid stream is directed into the slurry reservoir.