Modified cement kiln for burning combustible solid waste as supplemental fuel

• US 5,724,899 A
• Filed: 08/09/1994
• Issued: 03/10/1998
• Est. Priority Date: 11/23/1988
• Status: Expired due to Fees

• Current Assignee: Cadence Environmental Energy Inc., ASH Grove Cement Company (CRH PLC)
• Original Assignee: Cadence Environmental Energy Inc., ASH Grove Cement Company (CRH PLC)
• Inventors: Hansen, Eric R., Reese, Theodore J., Benoit, Michel R.
• Primary Examiner(s): Bennett, Henry A.
• Assistant Examiner(s): TINKER, SUSANNE CHRISTINE
• Application Number:
  US08/287,945
• Time in Patent Office: 1,309 Days
• Field of Search: 110/346, 110/246, 110/226, 110/238, 110/267, 432/103, 432/105, 432/106
• US Class Current: 110/346
• CPC Class Codes: C04B 7/4407 Treatment or selection of the fuel therefor, e.g. use of hazardous waste as secondary fuel fuels in general C10L; Use of particular energy sources, e.g. waste hot gases from other processes
• CPC Class Codes: C04B 7/4423 Waste or refuse used as fuel
• CPC Class Codes: C04B 7/4438 the fuel being introduced directly into the rotary kiln
• CPC Class Codes: F23G 2203/206 with charging ports in the sidewall
• CPC Class Codes: F23G 2205/16 using chute
• CPC Class Codes: F23G 2206/201 with an industrial furnace
• CPC Class Codes: F23G 2207/101 for temperature
• CPC Class Codes: F23G 2900/52002 Rotary drum furnaces with counter-current flows of waste and gas
• CPC Class Codes: F23G 5/08 having supplementary heating
• CPC Class Codes: F23G 5/20 having rotating or oscillating drums
• CPC Class Codes: F23G 5/448 in which the waste is fed in containers or the like
• CPC Class Codes: F23J 2217/101 Baghouse type
• CPC Class Codes: F23J 2217/102 electrostatic
• CPC Class Codes: F27B 2007/3247 through a lateral opening in the drum
• CPC Class Codes: F27B 7/32 Arrangement of devices for charging
• CPC Class Codes: F27B 7/34 Arrangements of heating devices
• CPC Class Codes: F27D 2099/0051 Burning waste as a fuel
• CPC Class Codes: Y02E 20/30 Technologies for a more efficient combustion or heat usage
• CPC Class Codes: Y02P 40/125 Fuels from renewable energy sources, e.g. waste or biomass

Abstract

A method and apparatus are described for environmentally sound usage of combustible solid waste in operating rotary cement kilns. A cement kiln is modified to contain a port in the rotary cylinder for delivery of combustible solid waste into the kiln for burning in contact with calcining mineral material. The port is provided with a closure and means for moving the closure between a port-opened and port-closed position at predetermined times during rotation of the kiln cylinder. The invention allows efficient use of solid waste as supplemental fuel in the cement manufacturing process.

Claims

1. A method for achieving environmentally sound disposal of combustible solid waste in an operating rotary cement kiln comprising a heated, rotating cylinder containing in-process mineral material, said method comprising the steps of

modifying the kiln by forming a port in the rotating cylinder at a point along the length of the kiln cylinder where the kiln gas temperature ranges from about 950°

C. to about 1200°

C., and providing a closure for said port and means for moving said closure between a port-opened and port-closed position at predetermined times during rotation of the cylinder and a drop tube communicating with said port and extending into the kiln cylinder to prevent contact of the in-process mineral materials with the closure; and

during kiln operation moving the port closure between a port-opened and port-closed position at predetermined times during kiln cylinder rotation and delivering the combustible waste through the port and drop tube into the rotary vessel when the closure is in the port-opened position.

2. A long wet or dry process cement kiln comprising a rotary cylinder for containing and heat processing a mineral material to form cement clinker, said kiln modified for the environmentally sound use of combustible solid waste having volatile components as supplemental fuel for the energy efficient production of said cement clinker, said modified cement kiln comprising a solid waste delivery port located at a point along the axial length of the rotary cylinder where, during kiln operation, the kiln gas temperature is sufficient to decompose the volatile components of the solid waste, a closure for the port, means for moving the closure between a port-opened and port-closed position at predetermined times during rotation of the kiln cylinder, and a drop tube communicating with the port and extending into the kiln cylinder to prevent mineral material in the kiln from contacting the closure.

3. The modified kiln of claim 2 wherein the solid waste delivery port is located at a point along the axial length of the cylinder where during kiln operation the solid waste delivered through the port burns in contact with calcining mineral material.

4. The modified cement kiln of claim 3 wherein the solid waste delivery port is located on the middle axial one-third portion of the cement kiln.

5. A method for charging combustible solid waste to a rotary cement kiln comprising a rotating kiln cylinder to burn said waste in contact with in-process mineral material, said method comprising the steps of

(1) modifying said cement kiln to provide a port in the rotating kiln cylinder at a point along its length where waste charged through the port will contact calcining mineral during kiln operation, said port having a closure movable between a port-closed and a port-opened position, and means for moving the closure between a port-closed and port-opened position at predetermined times during kiln cylinder rotation and further modifying said cement kiln to provide a drop tube communicating with said port and extending into the kiln cylinder to prevent the in-process mineral material from contacting the closure;

(2) positing combustible waste in alignment with said port during rotation of the kiln cylinder;

(3) moving the port closure to the port-opened position and allowing the waste to fall through the port to contact in-process mineral material;

(4) moving the port closure to the port-closed position; and

,

(5) repeating steps 2-4 during kiln operation.