# US 5,704,557 A · Method and apparatus for treatment of organic waste material

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- Number: US 5,704,557 A
- Document ID: US5704557A
- Status: Granted
- Kind: A
- Application number: 08/399,224
- Filed: 1995-03-06
- Granted: 1998-01-06
- Earliest claimed: 1995-03-06
- Assignees: Eli-Eco Logic Inc.
- Inventors: Douglas J. Hallett; Kelvin R. Campbell
- Web page: https://patentgrep.com/patent/US5704557A

## CPC

- B09C 1/06: thermally
- B09B 3/35: Shredding, crushing or cutting
- B09B 3/70: Chemical treatment, e.g. pH adjustment or oxidation (involving an extraction step B09B3/80)
- F23G 7/00: Incinerators or other apparatus for consuming industrial waste, e.g. chemicals (incinerator closets A47K11/02; oxidation of sludge C02F11/06; burners in general, burner details F23D; incinerating radioactive waste G21F9/00)
- F23G 7/14: of contaminated soil, e.g. by oil
- A62D 2203/10: Apparatus specially adapted for treating harmful chemical agents; Details thereof
- F23G 2201/50: Devolatilising; from soil, objects
- F23G 2201/80: Shredding
- B09C: RECLAMATION OF CONTAMINATED SOIL (gatherers for removing stone or the like from the soil A01B43/00; sterilising soil by steam A01G11/00; removing undesirable matter, e.g. rubbish, from the land E01H15/00)
- B09B: DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- F23G: CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- A62D: CHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS

## Abstract

A process and an apparatus for separation of relatively volatile from non-volatile material, typically an organic component of agglomerate waste material from an inorganic solid component of the waste. The process includes milling material in a container partially immersed or floating in a bath of molten material to break up the material, typically an agglomerate, and thermally releasing the relatively volatile component as vapor therefrom. The apparatus relates to a desorption vessel at least partially immersed in a molten tin bath for heat transfer from the bath to the interior of the vessel for desorption of the relatively volatile component from such material.

## Claims

### Claim 1

A method for separating a relatively volatile component of an agglomerate having a solid component, the method comprising milling the agglomerate in a container having relatively chemically inert solid particles located therein by movement of the container to mix the particles and agglomerate so as to break down the agglomerate to relatively small particles, wherein the container is at least partially immersed in a bath of molten material which is heated for transfer of energy from the bath to the interior of the container to promote release of the relatively volatile component as vapor from the solid particles.

### Claim 2 (depends on 1)

The method of claim 1, further comprising the step of capturing the vapor to preclude release thereof into the environment.

### Claim 3 (depends on 1)

The method of claim 1 wherein the molten material is molten tin.

### Claim 4

The method of 3 wherein the agglomerate is waste material and the relatively volatile component comprises organic material and the capturing step includes entraining organic vapor released from the waste material in a gaseous stream substantially free of oxygen.

### Claim 5 (depends on 4)

The method of claim 4 wherein the gaseous stream includes a reducing gas.

### Claim 6 (depends on 5)

The method of claim 5 wherein the reducing gas is selected from hydrogen, methane, ethane, propane, butane, natural gas or a combination thereof.

### Claim 7 (depends on 5)

The method of claim 5 wherein the gaseous stream includes nitrogen, steam, helium or a combination thereof.

### Claim 8 (depends on 5)

The method of claim 5 wherein the gaseous stream has an initial concentration of hydrogen of at least about 50 per cent.

### Claim 9 (depends on 3)

The method of claim 3 wherein there are relatively chemically inert solid particles located in the bottom of the container and the milling step includes moving the particles within the container to mix the particles and agglomerate so as to break down the agglomerate.

### Claim 10 (depends on 3)

The method of claim 3 wherein the container is a cylindrical drum having a central axis oriented generally horizontally and the milling step includes rotating the drum about the axis.

### Claim 11 (depends on 10)

The method of claim 10 wherein the drum has a length:diameter ratio of between about 3:1 and about 10:1.

### Claim 12 (depends on 11)

The method of claim 11 wherein the ratio is about 5:1.

### Claim 13 (depends on 10)

The method of claim 10 wherein the drum rotates between about 5 and about 30 revolutions per minute.

### Claim 14 (depends on 13)

The method of claim 13 wherein the drum rotates at a rate of about 15 revolutions per minute.

### Claim 15 (depends on 10)

The method of claim 10 wherein the drum is of stainless steel.

### Claim 16 (depends on 10)

The method of claim 10 wherein the drum contains relatively chemically inert solid bodies and the milling step includes rotating the drum such that the bodies and agglomerate intermingle so as to break relatively large pieces of the agglomerate down into relatively small pieces so as to enhance release of the relatively volatile component.

### Claim 17 (depends on 16)

The method of claim 16 wherein the solid bodies are spheres.

### Claim 18 (depends on 16)

The method of claim 16 wherein the solid bodies are metal balls.

### Claim 19 (depends on 18)

The method of claim 18 wherein the balls have a diameter between about one and six inches.

### Claim 20 (depends on 19)

The method of claim 19 wherein the diameter of the balls is about 11/2 inches.

### Claim 21 (depends on 1)

The method of claim 1 further comprising the step of entraining organic vapor released from the waste material with hydrogen.

### Claim 22 (depends on 1)

The method of claim 1 wherein the milling step includes breaking up the agglomerate to obtain relatively small and consistently sized particles.

### Claim 23 (depends on 1)

The method of claim 1 including maintaining the temperature in the container between about 300.degree. C. and about 600.degree. C.

### Claim 24 (depends on 23)

The method of claim 23 wherein the temperature is between about 500.degree. C. and about 600.degree. C.

### Claim 25 (depends on 1)

The method of claim 1 wherein the solid component has a residence time in the container of between about 5 and about 20 minutes.

### Claim 26 (depends on 25)

The method of claim 25 wherein the residence time of the solid component in the container is between about 10 minutes and about 15 minutes.

### Claim 27 (depends on 1)

The method of claim 1, further comprising the step of entraining the released vapor in a gaseous stream to transfer the vapor to a treatment zone.

### Claim 28 (depends on 27)

The method of claim 27 wherein the vapor is chemically reduced in the treatment zone.

### Claim 29 (depends on 27)

The method of claim 27 wherein the vapor is condensed to a liquid in the treatment zone.

### Claim 30

A thermal desorption unit, comprising:
a desorption vessel sealed from the surrounding atmosphere, for agglomerate material having a relatively volatile component to be thermally desorbed therefrom;
a molten tin bath, the vessel being at least partially immersed in the molten tin bath for heat transfer from the bath to the interior of the vessel for desorption of the relatively volatile component from the agglomerate material; and
means for milling the agglomerate within the vessel to enhance the thermal desorption of the relatively volatile component.

### Claim 31 (depends on 30)

The thermal desorption unit of claim 30, further comprising a heater for the bath, to act as a heat source for said heat transfer.

### Claim 32 (depends on 31)

The thermal desorption unit of claim 31, further comprising means for capturing desorbed gaseous material released from the agglomerate material.

### Claim 33 (depends on 32)

The thermal desorption unit of claim 32, wherein the capturing means includes a storage vessel connected to the desorption vessel by a valve, for transfer of gaseous material from the desorption vessel to the storage vessel.

### Claim 34 (depends on 32)

The thermal desorption unit of claim 32, further comprising means for entraining desorbed gaseous material released from the agglomerate material.

### Claim 35 (depends on 34)

The thermal desorption unit of claim 34, wherein the entraining means includes an inlet into the vessel for controlled entry thereinto of entrainment gases and an outlet from the vessel for controlled exit of gaseous matter.

### Claim 36 (depends on 31)

The thermal desorption unit of claim 31, wherein said desorption vessel is a cylindrical container having a central axis oriented horizontally and at least a lower portion of the container is immersed in the molten tin bath.

### Claim 37 (depends on 30)

The thermal desorption unit of claim 30, wherein said desorption vessel is a cylindrical container having a central axis oriented generally horizontally for rotation thereabout, and the milling means includes relatively chemically inert solid bodies located in the container for intermingling with the agglomerate material during rotation of the container to break down pieces of the agglomerate material into smaller sizes.

### Claim 38 (depends on 37)

The thermal desorption unit of claim 37 wherein the ratio of the horizontal length to the height of the vessel is between about 3 to 1 and about 10 to 1.

### Claim 39 (depends on 38)

The thermal desorption unit of claim 38 wherein the ratio is about 5 to 1.

### Claim 40 (depends on 37)

The thermal desorption unit of claim 37, wherein the desorption vessel has an entry port for the agglomerate material at a first axial end of the container and an exit port for relatively non-volatile non-desorbed materials at a second axial end of the container.

### Claim 41 (depends on 40)

The thermal desorption unit if claim 40, further comprising means for entraining desorbed gaseous material released from the agglomerate material.

### Claim 42 (depends on 41)

The thermal desorption unit of claim 41, wherein the entraining means includes an inlet into the vessel for entry thereinto of entrainment gases at the second axial end of the container and an outlet from the vessel for exit of gaseous matter from the first axial end of the container.

### Claim 43 (depends on 42)

The thermal desorption unit of claim 42, further comprising means for heating entrainment gases prior to entry into the vessel.

### Claim 44 (depends on 43)

The thermal desorption unit of claim 43, further comprising means for feeding the agglomerate material into the vessel through the entry port.

### Claim 45 (depends on 44)

The thermal desorption unit of claim 44, further comprising a hopper having a pair of compartments, each of the compartments being capable of connection to the feeding means while being sealed from the surrounding environment and the other compartment, to permit, alternately, agglomerate material to be fed from a first of the compartments into the desorption vessel while sealed from a second of the compartments and the surrounding environment while agglomerate material is being loaded into the second compartment and, agglomerate material to fed from the second compartment into the desorption vessel while sealed from the first compartment and the surrounding environment while agglomerate material is being loaded into the first compartment, to permit substantially continuous feeding of agglomerate material into the desorption vessel.

### Claim 46 (depends on 37)

The thermal desorption unit of claim 37, wherein said solid bodies are spherically shaped.

### Claim 47 (depends on 37)

The thermal desorption unit of claim 37, wherein said solid bodies are metal balls.

### Claim 48 (depends on 37)

The thermal desorption unit of claim 37, wherein said solid bodies are metal balls having a diameter between about one and six inches.