Integrated lime kiln process

Abstract

A process and system for recovering waste heat from a kiln used for lime or cement production. The system unifies the kiln, a waste heat recovery and power generation circuit and a dry scrubber for scrubbing the pollutants from the kiln offgas. Essentially, the system employs the boiler component of the waste heat recovery and power generation circuit as a heat exchanger to recover the waste heat from the kiln, which is used to drive the steam turbines. The heat absorption from the latter stage lowers the temperature of the kiln offgas sufficiently for optimum performance from the scrubber. The presence of lime particles in the offgas effectively protects the boiler tube surfaces from corrosion which would occur at optimum scrubber temperatures, and subsequently provides the lime required as a scrubbing medium for the dry scrubber. Further, the efficient scrubbing allows for the use of any fuel for firing the kiln inclusive of high sulphur content compounds. A process for effecting the technology is also provided.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a schematic illustration of the overall system according to one embodiment;

FIG. 2 is a schematic illustration of one embodiment of the waste heat recovery and power generation system used in the present invention;

FIG. 3 is a schematic illustration of a scrubber for use in the present invention; and

FIG. 4 is a schematic illustration of the scrubbing operation.

FIG. 5 is a schematic illustration of another embodiment.

Similar numerals are indicative of similar elements.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

Referring now to the drawings and in particular FIG. 1 and FIG. 2, shown is an overall schematic illustration of the process according to one embodiment of the present invention. The process is globally referenced by numeral 10 and provides a straight kiln 12 of the rotary variety as is known in the art having an inlet 14 and outlet 16. The kiln is supported by supports 18 and these supports also function to permit rotation of the kiln. Specific details of this arrangement will not be discussed as any suitable kiln known for lime formulation can be selected and will be readily apparent to those skilled in the art.

The discharge or offgas exiting outlet 16 is transferred into a waste heat recovery power generation circuit, globally denoted by numeral 20. The circuit includes a boiler or reboiler 22, turbine generator 24 which turbine generator is in electrical communication with an electrical storage means 26. A condenser 28 is provided to condense any excess steam and recirculate the steam as water back into boiler 22.

In greater detail, the boiler 22 receives the discharge gas or offgas from outlet 16 at an extremely high temperature, namely at a temperature between 400° F. and 2000° F. The discharge is streamed from the boiler 22 exiting the boiler, and denoted by numeral 30 is reduced to a temperature of between 300° F. and 400° F. and more particularly between 350° F. and 400° F. In this manner, the boiler 22 effectively recovers waste heat from the kiln and reduces the temperature of the stream to be scrubbed exiting at 30 a temperature which is essentially ideal for the maximum efficiency of the dry scrubber globally, denoted by the numeral 32.

The boiler functions, in effect, as a heat exchanger and exchanges the waste heat from the kiln to the water circulating within the boiler. This results in the generation of steam which is particularly useful to act as a drive means for turbine 24 for the generation of electricity.

Conventionally, boiler systems which are known to be particularly susceptible to corrosion unless operated under strict parameters, cannot be incorporated into such unit operations as set forth in FIG. 1. The low target exit temperature of the boiler needed to optimize the dry scrubber, combined with the use of sulfur-bearing fossil fuels, will lead to the formation of corrosive acidic compounds on the surface of the heat exchange surfaces. One skilled in the art would not be led to incorporate such a unit for such conditions.

It has been found that not only does the incorporation of the waste heat recovery circuit alleviate the problem with having to lower the temperature exiting the kiln 16, but also that the result is the production of electricity. In this arrangement, one skilled in the art would then be led to the conclusion that the particular fuel used to fire the kiln 12 and more particularly, the offgas 16 content would be critical for consideration in view of the fact that the boiler 22 is incorporated, which boiler 22 obviously incorporates tube networks. Normally, this would present significant difficulties in that the optimum temperature for the scrubber 32 is approximately 350° F. and this temperature requires the tube surface to be below the acid dew temperature of the sulfur compounds originating from the fuel.

By practicing the methodology as set forth herein, the LKD or CKD provided by the kiln creates a lime coating on the tubes in the boiler 22. This is an effective coating to prevent corrosion by the sulfur compounds when operating within the temperature range as noted herein and therefore permits the use of high sulfur bearing materials as a suitable fuel for firing the kiln.

As a particularly convenient feature, the LKD or CKD provides the scrubbing medium required to scrub the sulfur oxide and sulfur dioxide compounds from the stream. Referring now to FIG. 3, the dry scrubber is shown in greater detail where the inlet 34 of scrubber 32 is a venturi reactor 36 which introduces the scrubbing medium to the cooled offgas followed by particulate material captured in a baghouse 38. The final exhaust exiting the baghouse at 40 has an exhaust temperature of between 250° F. and 300° F. and more particularly 280° F. with the majority of the sulfur dioxide removed therefrom.

In respect of FIG. 4, shown is the overall scrubbing mechanism where a recycled particle 42 contains calcium hydroxide (hydrated lime) and water. In the mechanism, lime and free moisture coat the surface of the LKD or CKD and as the water evaporates the surface temperature temporarily drops below the acid dew temperature. The condensed acids combine with the lime and are therefore effectively neutralized. When the water has entirely evaporated, the particle heats to the mean gas temperature.

FIG. 5 illustrates yet a further possible embodiment of the system according to the present invention. The overall layout incorporates a number of parallel kilns with additional kilns being indicated by 12‘with subsequently increasing ’ (prime) indications. A stack 42 is provided to discharge the final exhaust from outlet 40 of the baghouse 38.

It will be appreciated by those skilled in the art that compound makeup will be added where needed during the process operation of the circuits noted herein.

The embodiments of the invention described above are intended to be exemplary only. The scope of the invention is therefore intended to be limited solely by the scope of the appended claims.

Claims

1. An integrated kiln process, comprising: providing waste heat recovery circuit; said circuit including a boiler and turbine generator;introducing kiln offgas into said boiler, said offgas containing kiln dust and particles;cooling said offgas to a temperature sufficient for introduction into a dry scrubber, absorbed heat within said boiler water being transferred to said turbine generator, whereby said boiler functions as a heat exchanger; andscrubbing said offgas.

2. The process as set forth in claim 1, wherein said lime particles accrue on heat exchange surfaces of said boiler to protect said surface from acidic attack at an optimum scrubber temperature.

3. The process as set forth in claim 1, wherein lime particles in said offgas scrub said offgas.

4. The process as set forth in claim 1, wherein said kiln is a cement kiln.

5. The process as set forth in claim 1, further including the step of providing a source of fuel to fire said kiln.

6. The process as set forth in claim 5, wherein said fuel comprises a fossil fuel.

7. The process as set forth in claim 5, wherein said fuel comprises alternate fuel.

8. The process as set forth in claim 5, wherein said fuel is a high sulphur content fuel.

9. A system for recovery of thermal energy from a kiln for power generation, comprising: a kiln;a waste heat recovery circuit including a boiler and a steam turbine, said boiler for receiving offgas from said kiln and generating steam for said turbine; anda dry scrubber for receiving cooled offgas at a temperature from said boiler suitable for optimizing scrubber efficiency.

10. The system as set forth in claim 9, wherein said kiln is a lime kiln.

11. The system as set forth in claim 9, wherein said kiln is a cement kiln.

12. The system as set forth in claim 9, wherein said system further includes a condenser and cooling tower.

13. A method for dry scrubbing gas generated from the combustion of high sulphur based fuel in a kiln process, comprising the steps of: providing a waste heat recovery circuit, said circuit including a boiler and turbine generator;providing a high sulphur content fuel for firing said kiln;introducing kiln offgas into said boiler, said offgas containing kiln dust and lime particles;collecting lime particles on heat exchange surfaces of said boiler to reduce acidic attack when said surfaces are at temperatures below acid dew point; andscrubbing said offgas.

14. The process as set forth in claim 13, wherein said scrubbing said offgas includes forming a sorbent with said lime particles.

15. The process as set forth in claim 13, wherein said forming said sorbent includes hydrating said lime particles in said offgas.

16. The process as set forth in claim 13, wherein said kiln offgas is introduced to said boiler at a temperature of between 400° F. and 2000° F.

17. The process as set forth in claim 13, wherein cooled offgas at boiler outlet is at a temperature of between 300° F. and 400° F.

18. The process as set forth in claim 13, wherein super heated steam is transferred to said turbine generator.

19. The process as set forth in claim 13, further including the step of providing boiler feed water to said boiler.