# US 5,619,936 A · Thermal desorption unit and processes

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- Number: US 5,619,936 A
- Document ID: US5619936A
- Status: Granted
- Kind: A
- Application number: 08/319,433
- Filed: 1994-10-06
- Granted: 1997-04-15
- Earliest claimed: 1993-05-28
- Assignees: Kleen Soil Technologies, L.C.
- Inventors: Clyde R. Veltmann
- Web page: https://patentgrep.com/patent/US5619936A

## CPC

- B09C 1/06: thermally
- F23G 5/006: {General arrangement of incineration plant, e.g. flow sheets}
- F23G 5/0276: {using direct heating}
- F23G 7/14: of contaminated soil, e.g. by oil
- F23J 15/04: using washing fluids {(scrubbers for removing solids only F23J15/022)}
- F23G 2201/50: Devolatilising; from soil, objects
- F23G 2201/80: Shredding
- F23G 2207/101: for temperature
- F23G 2207/40: Supplementary heat supply
- F23G 2208/10: Preventing or abating fire or explosion, e.g. by purging
- F23G 2209/10: Liquid waste
- F23G 2209/12: Sludge, slurries or mixtures of liquids
- F23G 2209/20: Medical materials
- F23G 2900/7011: Incinerating PCB-materials
- F23J 2215/20: Sulfur; Compounds thereof
- F23J 2215/60: Heavy metals; Compounds thereof
- F23J 2217/50: by cleaning fluids (washers or scrubbers)
- 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)
- F23G: CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23J: REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES (combustion apparatus for consuming smoke or fumes, e.g. exhaust gases, F23G7/06)

## Abstract

A thermal desorption apparatus for the vaporization of volatile organic compounds and other contaminants within solid and liquid materials, such as sand, gravel, soil, clay, and industrial sludge is disclosed. The apparatus includes a generally cylindrical kiln having a bellows seal located at an inlet port, an outlet port, a fire box, an after burner, a quench tube assembly, a water cyclone having a rotary cylinder and a recyclable water tank system and pump. The kiln also includes a sludge and liquid injection port for the processing of contaminated liquid materials, as well as a computer controlled regulating system and program for operation of the apparatus. The apparatus also includes an entry port screw auger and an exit port screw auger, as well as a series of stationary paddles affixed to the inside kiln walls.

## Claims

### Claim 1

A thermal desorption process for removing contaminants from contaminated material, said process comprising the steps of:
a) providing a thermal desorption apparatus comprising:
a rotating kiln having an entrance port disposed in a front end of said rotating kiln, an exit port disposed in a rear end of said rotating kiln, and a vapor port disposed toward the top of at least one of the front or rear ends of said rotating kiln;
a quench tube having first and second ends, an interior chamber with at least one spray nozzle disposed within, an inlet disposed in said first end of said quench tube, and an outlet disposed in said second end of said quench tube, wherein said inlet is in communication with the vapor port of the rotating kiln, and wherein at least one spray nozzle is oriented in said interior chamber to face the inlet of said quench tube;
a water cyclone comprising:
an outer chamber having a perimeter, a first end, a second end, and at least one water nozzle disposed within,
an inlet tube disposed in the perimeter of said outer chamber and being in communication with the quench tube outlet,
a vapor outlet tube disposed in the first end of said water cyclone outer chamber,
an interior vapor outlet tube connected to said vapor outlet tube and being disposed within said water cylcone outer chamber, and having at least one water nozzle disposed within, said at least one water nozzle oriented to face the second end of said water cyclone outer chamber, and
a bottom outlet disposed in said second end of said water cyclone outer chamber;
b) introducing contaminated material into the rotating kiln;
c) heating the contaminated material inside the rotating kiln with a burner flame to vaporize contaminants and form particulate exit materials;
d) removing the particulate exit materials from the exit port of the rotating kiln, and removing the vaporized contaminants from the vapor port of the rotating kiln;
e) measuring at least one of the temperature of the particulate exit materials, the temperature of the kiln, or the presence of contaminants in the particulate exit materials;
f) adjusting at least one of a burner flame temperature, rotation speed of the kiln, or a relative elevation of the front end of said rotating kiln with respect to the rear end of said rotating kiln based on at least one of the measurement of the temperature of the particulate exit materials, the temperature of the kiln, or the presence of contaminants in the particulate exit materials;
g) oxidizing the vaporized contaminants to form a gas;
h) introducing the gas into the inlet of the quench tube and subjecting the gas to a spray of water from the at least one water nozzle disposed in said interior chamber and oriented to face the inlet of said quench tube;
i) removing the gas from the outlet of the quench tube, introducing the gas into the inlet tube of the water cyclone, and subjecting the gas to a spray of water from the at least one water nozzle located in the outer chamber of the water cyclone;
j) removing the gas from the vapor outlet tube of the water cylcone, wherein the gas is subjected to a spray of water from the at least one spray nozzle disposed in the interior vapor outlet tube and oriented to face the second end of the water cyclone outer chamber.

### Claim 2 (depends on 1)

The process of claim 1, further comprising the steps of analyzing the contaminated material prior to the step of heating the contaminated material inside the rotating kiln, and adjusting the rotating kiln temperature by varying at least one of a burner flame temperature, rotation speed of the kiln, or a relative elevation of the front end of the rotating kiln with respect to the rear end of the rotating kiln.

### Claim 3 (depends on 1)

The process of claim 1, wherein the contaminated material is introduced into the entrance port of the rotating kiln at a rate of from about 20 tons to about 40 tons of contaminated material per hour.

### Claim 4 (depends on 1)

The process of claim 1, wherein the contaminated material is a solid and wherein the process comprises a first step of reducing the solid material to particles not more than 11/2 inches in diameter.

### Claim 5 (depends on 1)

The process of claim 1, wherein the step of oxidizing comprises oxidizing the vaporized contaminants at a temperature ranging from about 1400 .degree. F. to about 2600 .degree. F.

### Claim 6 (depends on 1)

The process of claim 1, wherein the step of heating comprises heating the material inside the rotating kiln to a temperature of about 1000.degree. F. or greater.

### Claim 7 (depends on 6)

The process of claim 6, wherein the step of providing a thermal desorption apparatus comprises the step of providing an insulated rotating kiln constructed of 310 stainless steel and further comprising a bellows seal disposed at at least one of the front or rear ends of the kiln.

### Claim 8 (depends on 1)

The process of claim 1, wherein the contaminants comprise at least one of heavy metals, hydrocarbons, polychlorinated biphenyls, or a mixture thereof.

### Claim 9 (depends on 8)

The process of claim 8, wherein the heavy metals comprise at least one of mercury, lead, or a mixture thereof.

### Claim 10 (depends on 1)

The process of claim 1, wherein the particulate exit materials contain less than about 1% contaminants.

### Claim 11 (depends on 1)

The process of claim 1, wherein the step of providing a thermal desorption apparatus comprises the step of providing a rotating kiln having a sludge and liquid injection port disposed in the front end of the rotating kiln, and wherein the step of introducing contaminated material into the rotating kiln comprises introducing contaminated sludge or liquid material into said sludge and liquid injection port disposed in the front end of the rotating kiln.

### Claim 12 (depends on 11)

The process of claim 11 wherein said contaminated sludge or liquid material comprises at least one of industrial sludge, sewage, or a mixture thereof.

### Claim 13 (depends on 1)

The process of claim 1, wherein the step of oxidizing comprises the step of introducing the vaporized contaminants into an afterburner, said afterburner having an inlet in communication with the vapor port of the rotating kiln and having an outlet in communication with the inlet of the quench tube.

### Claim 14 (depends on 1)

The process of claim 1, wherein the step of removing the gas from the outlet of the quench tube comprises the step of introducing said gas into a wash box having an inlet in communication with the outlet of the quench tube, and an outlet in communication with the inlet tube of the water cyclone.

### Claim 15 (depends on 1)

The process of claim 1, wherein the step of removing the particulate exit materials comprises the step of introducing said particulate exit materials into a front end of a fire box, said front end of said fire box being in communication with the rear end of the rotating kiln, and said fire box having a discharge tube disposed in communication with a rear end of the fire box.

### Claim 16 (depends on 15)

The process of claim 15, wherein the step of removing the particulate exit materials comprises the step of subjecting said particulate exit materials to water spray from at least one spray nozzle positioned in the discharge tube of the fire box.

### Claim 17 (depends on 14)

The process of claim 14, wherein the step of introducing the gas into a washbox comprises the steps of separating water from said gas, removing said water to at least one tank from said washbox through a drain disposed toward a bottom of said washbox and being in communication with said at least one tank, and filtering said water for reuse in the process through a filter disposed in communication with said tank.

### Claim 18 (depends on 1)

The process of claim 1, wherein the step of removing the gas from the vapor outlet tube of the water cyclone comprises the steps of:
removing water from the bottom outlet of the water cyclone through a rotary assembly disposed in communication with said bottom outlet,
introducing said water into at least one filtering tank disposed in communication with the bottom outlet of the water cyclone; and
filtering said water through a filter disposed in communication with the bottom outlet of the water cyclone for reuse in the process.

### Claim 19 (depends on 1)

The process of claim 1, wherein the step of subjecting the gas to a spray of water in the quench tube comprises the step of controlling the spray of water with a computer.

### Claim 20 (depends on 1)

The process of claim 1, wherein the step of heating the contaminated material inside the rotating kiln comprises the step of agitating said contaminated material inside said kiln with stationary paddles disposed in contact with inside walls of said kiln.

### Claim 21 (depends on 20)

The process of claim 20, wherein a longitudinal axis of each stationary paddle is longitudinally disposed so as to form an angle with a longitudinal axis of the rotating kiln, said angle oriented in such a way to move liquid or particulate exit materials toward the exit port of the rotating kiln.

### Claim 22 (depends on 1)

The process of claim 1, wherein the step of providing a thermal desorption process comprises the step of providing a thermal desorption apparatus that is portable.

### Claim 23 (depends on 1)

The process of claim 1, wherein the step of providing a thermal desorption apparatus comprises providing a rotating kiln having at least one wiper blade disposed adjacent to the entrance port of the rotating kiln.

### Claim 24

A thermal desorption process for removing contaminants from contaminated material, said process comprising the steps of:
a) providing a thermal desorption apparatus comprising:
a rotating kiln having an entrance port disposed in a front end of said rotating kiln, an exit port disposed in a rear end of said rotating kiln, and a vapor port disposed toward the top of said rotating kiln;
a quench tube having first and second ends, an interior chamber with at least one spray nozzle disposed within, an inlet disposed in said first end of said quench tube, and an outlet disposed in said second end of said quench tube, wherein said inlet is in communication with the vapor port of the rotating kiln, and wherein at least one spray nozzle is oriented in said interior chamber to face the inlet of said quench tube;
a water cyclone comprising:
an outer chamber having a perimeter, a first end, a second end, and at least one water nozzle disposed within,
an inlet tube disposed in the perimeter of said outer chamber and being in communication with the quench tube outlet,
a vapor outlet tube disposed in the first end of said water cyclone outer chamber,
an interior vapor outlet tube connected to said vapor outlet tube and being disposed within said water cylcone outer chamber, and having at least one water nozzle disposed within, said at least one water nozzle oriented to face the second end of said water cyclone outer chamber, and
a bottom outlet disposed in said second end of said water cyclone outer chamber;
b) introducing contaminated material into the rotating kiln;
c) heating the contaminated material inside the rotating kiln to vaporize contaminants and form particulate exit materials;
d) removing the particulate exit materials from the exit port of the rotating kiln, and removing the vaporized contaminants from the vapor port of the rotating kiln;
e) adjusting a relative elevation of the front end of said rotating kiln with respect to the rear end of said rotating kiln;
f) oxidizing the vaporized contaminants to form a gas;
g) introducing the gas into the inlet of the quench tube and subjecting the gas to a spray of water from the at least one water nozzle disposed in said interior chamber and oriented to face the inlet of said quench tube;
h) removing the gas from the outlet of the quench tube, introducing the gas into the inlet tube of the water cyclone, and subjecting the gas to a spray of water from the at least one water nozzle located in the outer chamber of the water cyclone;
i) removing the gas from the vapor outlet tube of the water cylcone, wherein the gas is subjected to a spray of water from the at least one spray nozzle disposed in the interior vapor outlet tube and oriented to face the second end of the water cyclone outer chamber.

### Claim 25

A portable thermal desorption process for removing contaminants from contaminated material, said process comprising the steps of:
a) providing a portable thermal desorption apparatus comprising:
an elongated cylindrical rotating kiln having an entrance port disposed in a front end of said rotating kiln, an exit port disposed in a rear end of said rotating kiln, a sludge and liquid injection port disposed in the front end of said rotating kiln, a vapor port disposed toward the top of said rotating kiln, stationary paddles affixed to inside walls of said kiln, and one or more flame burners disposed in position to heat the kiln, said elongated rotating kiln forming an angle with a longitudinal axis of the apparatus, wherein a temperature of the flame burners, rotation speed and angle of the kiln are adjustable; and
a trailer for transporting said apparatus;
b) introducing contaminated material into the rotating kiln;
c) heating and agitating the contaminated material inside the rotating kiln to vaporize contaminants and form particulate exit materials;
d) removing the particulate exit materials from the exit port of the rotating kiln, and removing the vaporized contaminants from the vapor port of the rotating kiln;
e) analyzing the particulate exit materials for the presence of contaminants;
f) adjusting at least one of a burner temperature, rotation speed or angle of the kiln based on the analysis of the particulate exit materials.

### Claim 26

A portable thermal desorption process for removing contaminants from contaminated material, said process comprising the steps of:
a) providing a portable thermal desorption apparatus comprising:
a quench tube having first and second ends, an interior chamber with at least one spray nozzle disposed within, an inlet disposed in said first end of said quench tube, and an outlet disposed in said second end of said quench tube, and wherein at least one spray nozzle is oriented in said interior chamber to face the inlet of said quench tube;
a water cyclone comprising:
an outer chamber having a perimeter, a first end, a second end, and at least one water nozzle disposed within,
an inlet tube disposed in the perimeter of said outer chamber and being in communication with the quench tube outlet,
a vapor outlet tube disposed in the first end of said water cyclone outer chamber,
an interior vapor outlet tube connected to said vapor outlet tube and being disposed within said water cylcone outer chamber, and having at least one water nozzle disposed within, said at least one water nozzle oriented to face the second end of said water cyclone outer chamber;
a bottom outlet disposed in said second end of said water cyclone outer chamber, and
a trailer for transporting said apparatus;
b) introducing gas formed from the oxidation of vaporized solid or liquid contaminants into the inlet of the quench tube, and subjecting said gas to a spray of water from the at least one water nozzle disposed in said interior chamber and oriented to face the inlet of said quench tube;
c) removing the gas from the outlet of the quench tube, introducing the gas into the inlet tube of the water cyclone, and subjecting the gas to a spray of water from the at least one water nozzle located in the outer chamber of the water cyclone; and
d) removing the gas from the vapor outlet tube of the water cylcone, wherein the gas is subjected to a spray of water from the at least one spray nozzle disposed in the interior vapor outlet tube and oriented to face the second end of the water cyclone outer chamber.