Method for regulating combustion processes, particularly for the production of cement in a rotary kiln

Claim 5

A method of regulating a calcining process, according to claim 2, wherein the step of measuring and generating a signal representing heat loss of the kiln is defined as comprising the steps of: measuring the sleeve temperature of the kiln; measuring the furnace sleeve pyrometer setting; and generating the kiln heat loss signal in response to the kiln temperature and sleeve pyrometer setting.

Claim 6

A method of regulating a calcining process according to claim 2, wherein the step of measuring and generating a signal representing clinker waste heat is defined by the steps of: measuring the clinker temperature; measuring the clinker flow; measuring the clinker specific heat content; and generating the clinker waste heat signal in response to clinker temperature, flow and specific heat content.

Claim 7

A method of regulating a calcining process according to claim 2, wherein the step of measuring and generating a signal representing exhaust gas heat is defined by the steps of: measuring the exhaust gas temperature; measuring the quantity of exhaust gas; measuring the specific heat content of the exhaust gas by comparing the exhaust gas temperature with predetermined temperature-heat content curves; and generating the exhaust gas heat signal in response to the temperature, quantity and specific heat content of the exhaust gas.

Claim 8

A method of regulating a calcining process according to claim 2, wherein the step of measuring and generating a signal representing clinker formation heat is defined by the steps of: analyzing the content of the raw material; and generating a theoretical clinker formation heat signal in response to material analysis and the measured flow of raw material.

Claim 9

A method of regulating a calcining process according to claim 2, wherein the step of measuring and generating a signal representing heat recovered from the fuel is defined by the steps of: analyzing the fuel content; measuring the fuel flow; and generating the signal representing heat recovered from the fuel in response to the fuel analysis and quantity of fuel delivered to the kiln.

Claim 10

A method of regulating a calcining process according to claim 2, wherein the step of measuring and generating a signal representing heat recovered from the cooler part of the kiln is defined by the steps of: measuring the quantity of air passing from the cooler into the kiln; measuring the temperature of the air flowing from the cooler into the kiln; measuring the specific heat content of the air flowing from the cooler into the kiln; and generating the signal representing heat recovered from the cooler in response to the temperature, specific heat content and quantity of air flowing from the cooler into the kiln.

Claim 11

The method of regulating a calcining process according to claim 8, wherein the step of measuring the temperature of the air flowing from the cooler into the kiln is defined as: measuring the average value of temperatures at spaced points of the air flowing from the cooler into the kiln; and applying the average temperature in the formation of the signal representing heat recovered from the cooler.

Claim 12

A method of regulating a calcining process according to claim 2 wherein the step of measuring the quantity of raw material being processed and generating a signal representing that quantity is defined by the steps of: measuring the mass of raw material; measuring the speed of rotation of the kiln; measuring the linear strain on a cooler grate at the output of the kiln into the cooler; measuring the air pressure in the cooler chamber; measuring the clinker flow at the output of the cooler; and generating a raw material quantity signal in response to these measured parameters.

Claim 13

A method of regulating a calcining process according to claim 2, wherein the step of applying the characteristic value signal to apparatus for controlling regulation is further defined by the step of: applying the characteristic value signal to apparatus which maintains the operating capacity of the combustion gases constant at a predetermined value.

Claim 14

A method of regulating a calcining process according to claim 11 comprising the step of: adjusting the predetermined operating capacity value with respect to the operating capacity measured at the output.

Claim 15

A method of regulating a calcining process according to claim 11, comprising the step of changing the predetermined value of the operating capacity to control the characteristics of the calcined material.

Claim 16

A method of regulating a calcining process according to claim 2, wherein each step of measuring includes the step of sensing a parameter at a specific operating point in the system and generating a signal representative of that parameter, and further comprising the step of determining the plausibility of the correspondingly generated signal and substituting theoretical value signals for those signals which are determined not to be plausible.

Claim 17

A method of regulating a calcining process according to claim 14, wherein the step of substituting is further defined as replacing non-plausible signals with previously measured values.

Claim 18

A method of regulating a calcining process according to claim 14, wherein the step of substituting is defined as replacing signals found not to be plausible with signals generated at points in the system which have a similar information content.

Claim 19

A method of regulating a calcining process according to claim 2, wherein the step of measuring and generating a signal representing heat loss of the kiln is defined as comprising the steps of: measuring the sleeve temperature of the furnace wall of the kiln at different zones of the kiln; measuring a furnace sleeve pyrometer setting; and generating the kiln heat loss signal in response to the kiln temperatures in those zones and the sleeve pyrometer setting.

Claim 20

A method of regulating a calcining process according to claim 2, wherein the step of measuring and generating a signal representing clinker waste heat is defined by the steps of: measuring the clinker temperature; measuring the clinker flow; measuring the clinker specific heat content by comparing the clinker temperature to heat content data; and generating the clinker waste heat signal in response to clinker temperature, clinker flow and clinker specific heat content.

Claim 21

A method of regulating a calcining process according to claim 2, comprising the steps of: measuring the sintering temperature; measuring the flue gas temperature upon combustion; and subtracting the sintering temperature from the combustion flue gas temperature to obtain the temperature level at which heat is made available to the process.

Claim 22

A method of regulating a calcining process according to claim 19, wherein the step of measuring the flue gas temperature upon combustion comprises the steps of: detecting the air content of the flue gas; comparing the air content of the flue gas with predetermined data to obtain the enthalpy of the flue gas.

Claim 23

A method of regulating a calcining process according to claim 2, wherein the step of measuring the quantity of raw material being processed and generating a signal representing that quantity comprises the steps of: measuring the quantity of pulverized raw material being added to the system; measuring the migration speed and distribution of the pulverized raw material through the kiln; and measuring a clinkering factor.

Claim 24

A method of regulating a calcining process according to claim 21, wherein the quantity of raw material being processed is adjusted by the step of: measuring the linear strain of the cooler grate and the air pressure within the cooler and generating corresponding signals, and applying the corresponding signals to a unit which calculates the material flow through the burning zone of the kiln.

Claim 25

A method of regulating a calcined process according to claim 21, wherein the clinker factor is defined as and is formed by a proportion of the measured quantity of charged pulverized raw material flow and the measured clinker flow.

Claim 26

In a rotary furnace installation of the type which receives raw material and exhausts flue gases through a cyclone heat exchanger connected to an inlet chamber of the furnace and which has a regulatable fuel burning system, and which includes an outlet end feeding a regulatable drive type grate cooler, a regulating system for controlling the calcining process, comprising: means for measuring and generating a signal representing heat loss of the furnace; means for measuring and generating a signal representing clinker waste heat; means for measuring and generating a signal representing exhaust gas heat; means for measuring and generating a signal representing heat recovered from the fuel; means for measuring and generating a signal representing heat recovered from the cooler; means for measuring the quantity of raw material being processed in the furnace and generating a signal representing that quantity; means for receiving the above-mentioned signals and in response thereto generating a characteristic value signal which indicates the exergy of the calcining process; and means for applying the characteristic value signal to the regulatable fuel feed to control the burning operation within the furnace.

Claim 27

In a rotary furnace installation of the type which receives raw material and exhausts flue gases through a cyclone heat exchanger connected to an inlet chamber of the furnace and which has a regulatable fuel burning system, and which includes an outlet end feeding a regulatable drive type grate cooler, a regulating system for controlling the calcining process, comprising: means for measuring and generating a signal representing heat loss of the furnace; means for measuring and generating a signal representing clinker waste heat; means for measuring and generating a signal representing exhaust gas heat; means for measuring and generating a signal representing heat recovered from the fuel; means for measuring and generating a signal representing heat recovered from the cooler; means for measuring the quantity of raw material being processed in the furnace and generating a signal representing that quantity; means for receiving the above-mentioned signals and in response thereto generating a characteristic value signal which indicates the exergy of the calcining process; and means for applying the characteristic value signal to the regulatable fuel feed to control the burning operation within the furnace.

Claim 28

A rotary furnace installation according to claim 24 comprising: a blower for exhausting gas from the cyclone heat exchanger; and blower control means connected to receive the characteristic value signal for controlling blower operation and thus preheating of the raw material fed into the installation.

Claim 29

In a rotary furnace installation according to claim 24, comprising: means for controlling the feeding of raw material into the installation in response to the characteristic value signal, thereby controlling the quantity of raw material being processed in the installation.

Claim 30

In a rotary furnace installation of the type which receives pulverized raw material and exhausts flue gases through a cyclone heat exchanger, via a blower, connected to an inlet chamber of the furnace through which the raw material is received, which has a fuel burning system including a fuel flow regulator, which includes an outlet end feeding a regulatable drive type grate cooler, and in which the furnace is rotated by a drive mechanism, a regulating system for controlling the calcining process, comprising: first means for measuring and generating a signal representing heat loss of the furnace; second means for measuring and generating a signal representing clinker waste heat; third means for measuring and generating a signal representing exhaust gas heat; fourth means for measuring and generating a signal representing heat recovered from the fuel; fifth means for measuring and generating a signal representing heat recovered from the cooler; sixth means for measuring the quantity of raw material being processed in the furnace and generating a signal representing that quantity; seventh means responsive to the above-mentioned signals to generate a characteristic value signal indicative of the exergy of the calcining process; and regulating means responsive to the characteristic value signal to control the fuel regulator, the blower and the rotary drive mechanism of the furnace.

Claim 31

In a rotary furnace installation of the type which receives pulverized raw material and exhausts flue gases through a cyclone heat exchanger, via a blower, connected to an inlet chamber of the furnace through which the raw material is received, which has a fuel burning system including a fuel flow regulator, which includes an outlet end feeding a regulatable drive type grate cooler, and in which the furnace is rotated by a drive mechanism, a regulating system for controlling the calcining process, comprising: first means for measuring and generating a signal representing heat loss of the furnace; second means for measuring and generating a signal representing clinker waste heat; third means for measuring and generating a signal representing exhaust gas heat; fourth means for measuring and generating a signal representing heat recovered from the fuel; fifth means for measuring and generating a signal representing heat recovered from the cooler; sixth means for measuring the quantity of raw material being processed in the furnace and generating a signal representing that quantity; seventh means responsive to the above-mentioned signals to generate a characteristic value signal indicative of the exergy of the calcining process; and regulating means responsive to the characteristic value signal to control the fuel regulator, the blower and the rotary drive mechanism of the furnace.

Claim 32

In a rotary furnace installation according to claim 27, wherein said regulating means comprises: means for producing a fuel setting signal from the characteristic value signal; and means for comparing the fuel setting signal with a predetermined theoretical value and applying deviations therebetween to adjust the fuel setting.

Claim 33

In a rotary furnace installation according to claim 28, wherein said regulating means further comprises: a regulating algorithm device which is responsive to the fuel setting signal to produce a control signal for controlling raw material feed.

Claim 34

In a rotary furnace installation according to claim 28, comprising: means for adjusting the predetermined value of the fuel setting including means for measuring and generating a signal representing the CO content of the exhaust gases, means for measuring and generating a signal representing the energy coefficient of the O 2 flowing from the furnace into the heat exchanger, means for measuring and generating a signal representing the energy coefficient of the CO 2 flowing from the furnace into the heat exchanger, and means for receiving the CO and the O 2 and CO 2 signals and generating an adjustment signal in response thereto.

Claim 35

In a rotary furnace installation according to claim 27, wherein said regulating means produces setting signals for the controlled elements, and comprising means for limiting the magnitude of such signals.

Claim 38

The method set forth in claim 32, comprising the steps of: measuring the excess air upon combustion; and controlling the blower in accordance with the amount of excess air.

Claim 39

The method of regulating a calcining process according to claim 33 wherein the step of measuring the excess air comprises the steps of: analyzing the gas flowing from the furnace into the heat exchanger; analyzing the exhaust gas flowing out of the blower; and comparing the analyzed gas values to predetermined values to obtain a coefficient of excess air.

Claim 40

In a rotary furnace installation of the type which receives pulverized raw material and exhaust flue gases through a cyclone heat exchanger, via a blower, connected to an inlet chamber of the furnace through which the raw material is received, which has a fuel burning system including a fuel flow regulator, which includes an outlet end feeding a regulatable drive cooler, and in which the furnace is rotated by a drive mechanism and is fed raw material by a feed mechanism, a regulating system for controlling the calcining process, comprising: means for measuring the air content of the fuel; means for measuring the CO 2 content of the pulverized raw material; means for measuring the clinker stream passing out of the cooler; means for measuring the pulverized raw material being fed into the installation; means for measuring the speed of rotation of the furnace; means for measuring the linear strain of the material flow through the cooler; means for measuring the pressure within the cooler; means providing a set point representing the sintering temperature; means for analyzing the fuel being fed; means for measuring the average air temperature from the outlet of the furnace to the inlet of the cooler; means for measuring the flow of fuel; means for analyzing the raw material being fed; means for determining the O 2 content of the flue gas; means for determining the CO content of the flue gas; means for determining the O 2 energy coefficient of the flue gas at the inlet of the furnace and outlet of the heat exchanger; means for determining the CO 2 energy coefficient of the flue gas at the inlet of the furnace and the outlet of the heat exchanger; means for determining the exhaust gas temperature; means for determining the clinker temperature at the outlet of the furnace; means for determining the sleeve temperature of the furnace; means for determining the furnace drive power; means providing a predetermined temperature profile through the furnace; means for determing the clinker-free lime content at the outlet of the cooler, each of the above parameter determinations and settings being constantly obtained; and means responsive to the above parameters to generate a characteristic value signal which describes the exergy of the calcining process.

Claim 41

In a rotary furnace installation of the type which receives pulverized raw material and exhaust flue gases through a cyclone heat exchanger, via a blower, connected to an inlet chamber of the furnace through which the raw material is received, which has a fuel burning system including a fuel flow regulator, which includes an outlet end feeding a regulatable drive cooler, and in which the furnace is rotated by a drive mechanism and is fed raw material by a feed mechanism, a regulating system for controlling the calcining process, comprising: means for measuring the air content of the fuel; means for measuring the CO 2 content of the pulverized raw material; means for measuring the clinker stream passing out of the cooler; means for measuring the pulverized raw material being fed into the installation; means for measuring the speed of rotation of the furnace; means for measuring the linear strain of the material flow through the cooler; means for measuring the pressure within the cooler; means providing a set point representing the sintering temperature; means for analyzing the fuel being fed; means for measuring the average air temperature from the outlet of the furnace to the inlet of the cooler; means for measuring the flow of fuel; means for analyzing the raw material being fed; means for determining the O 2 content of the flue gas; means for determining the CO content of the flue gas; means for determining the O 2 energy coefficient of the flue gas at the inlet of the furnace and outlet of the heat exchanger; means for determining the CO 2 energy coefficient of the flue gas at the inlet of the furnace and the outlet of the heat exchanger; means for determining the exhaust gas temperature; means for determining the clinker temperature at the outlet of the furnace; means for determining the sleeve temperature of the furnace; means for determining the furnace drive power; means providing a predetermined temperature profile through the furnace; means for determing the clinker-free lime content at the outlet of the cooler, each of the above parameter determinations and settings being constantly obtained; and means responsive to the above parameters to generate a characteristic value signal which describes the exergy of the calcining process.

Claim 42

In a rotary furnace installation according to claim 35, comprising: means connected to each of the parameter measuring means for receiving and determining the plausibility of the measured values.

Claim 43

In a rotary furnace installation according to claim 36, comprising means for substituting plausible values in response to receipt of nonplausible values.

Claim 44

In a rotary furnace installation according to claim 36, comprising: means connected between said plausibility means and the plurality of parameter measuring means for forming characteristic values of the individual quantities of heat, temperature level of the process, material stream flow and fuel flow.

Claim 45

In a rotary furnace installation according to claim 35, wherein said means for measuring the clinker temperature comprises pyrometrically operating means.

Claim 46

In a rotary furnace installation according to claim 35, wherein said means for measuring the air and exhaust gas temperatures each comprise thermo-element measuring means.

Claim 47

In a rotary furnace installation according to claim 35, comprising means connected to said means for determining the O 2 content of the flue gas, to said means for determining the CO content of the flue gas, to said means providing a set point representing the sintering temperature, and to said means for measuring the exhaust gas temperature, and responsive to the operation thereof to form a signal indicating the temperature level of the process.

Claim 48

In a rotary furnace installation according to claim 35, comprising: regulating means responsive to the characteristic value signal to regulate the settings of the blower, the furnace drive mechanism, and the fuel flow regulator by producing and feeding corresponding setting signals thereto; and means for limiting the setting signals.

Claim 49

In a calcincing process which utilizes a rotary furnace installation of the type which receives pulverized raw material and exhaust flue gases through a cyclone heat exchanger by way of a blower connected to an inlet chamber of the furnace through which the raw material is received, which has a fuel burning system including a fuel flow regulator, which includes an outlet end feeding a cooler, and in which the furnace is rotated by a drive mechanism and is fed raw material by a feed mechanism, the improvement therein comprising the steps of: measuring the exergy of each stream of heat produced directly or indirectly by the combustion gases; combining the exergies of the streams of heat to obtain the exergy of the system as the sum of all of the exergies sensing a plurality of operating parameters for the cooler, the rotary furnace and the heat exchanger which would result in a change in individual exergies; and varying at least one of the operating parameters of quantity of fuel feed, speed of furnace rotation, quantity of exhaust gas flow and quantity of raw material feed in response to detection of a change in an operating parameter which would change an individual exergy, while maintaining the total system exergy constant.

Claim 50

In a calcincing process which utilizes a rotary furnace installation of the type which receives pulverized raw material and exhaust flue gases through a cyclone heat exchanger by way of a blower connected to an inlet chamber of the furnace through which the raw material is received, which has a fuel burning system including a fuel flow regulator, which includes an outlet end feeding a cooler, and in which the furnace is rotated by a drive mechanism and is fed raw material by a feed mechanism, the improvement therein comprising the steps of: measuring the exergy of each stream of heat produced directly or indirectly by the combustion gases; combining the exergies of the streams of heat to obtain the exergy of the system as the sum of all of the exergies sensing a plurality of operating parameters for the cooler, the rotary furnace and the heat exchanger which would result in a change in individual exergies; and varying at least one of the operating parameters of quantity of fuel feed, speed of furnace rotation, quantity of exhaust gas flow and quantity of raw material feed in response to detection of a change in an operating parameter which would change an individual exergy, while maintaining the total system exergy constant.

Claim 51

The improved process as set forth in claim 43, and further comprising the steps of: measuring the free residual lime content of the clinker; and modifying the total exergy control in accordance with the free residual lime content of the clinker.

Claim 52

In a calcincing process which utilizes a rotary furnace installation of the type which receives pulverized raw material and exhaust flue gases through a heat exchanger by way of a blower connected to an inlet chamber of the furnace through which the raw material is received, which has a fuel burning system including a fuel flow regulator, which includes an outlet end feeding a cooler, and in which the furnace is rotated by a drive mechanism and is fed raw material by a feed mechanism, the improvement therein comprising the steps of: calculating a model from the available heat introduced into the installation including that derived from the fuel, the exhaust gases and the raw material; storing the model in a computer and calculating an exergy index from the heat components of the model; measuring the actual exergy of each stream of heat produced directly or indirectly by combustion in the installation; combining the actual exergies of the streams of heat to obtain an actual exergy index of the system as the sum of all the actual exergies; comparing the actual exergies with the exergy components of the model to forecast a trend of the change of the individual actual exergies; and varying at least one of the operating parameters of quantity of fuel feed, the quantity of exhaust gas flow and the quantity of raw material feed when the actual exergy index is outside predetermined limits of the calculated index to compensate for the forecasted trend.

Claim 53

In a calcincing process which utilizes a rotary furnace installation of the type which receives pulverized raw material and exhaust flue gases through a heat exchanger by way of a blower connected to an inlet chamber of the furnace through which the raw material is received, which has a fuel burning system including a fuel flow regulator, which includes an outlet end feeding a cooler, and in which the furnace is rotated by a drive mechanism and is fed raw material by a feed mechanism, the improvement therein comprising the steps of: calculating a model from the available heat introduced into the installation including that derived from the fuel, the exhaust gases and the raw material; storing the model in a computer and calculating an exergy index from the heat components of the model; measuring the actual exergy of each stream of heat produced directly or indirectly by combustion in the installation; combining the actual exergies of the streams of heat to obtain an actual exergy index of the system as the sum of all the actual exergies; comparing the actual exergies with the exergy components of the model to forecast a trend of the change of the individual actual exergies; and varying at least one of the operating parameters of quantity of fuel feed, the quantity of exhaust gas flow and the quantity of raw material feed when the actual exergy index is outside predetermined limits of the calculated index to compensate for the forecasted trend.