US3659829A - Method for adjustment of the heat generating process in a rotary kiln with a heat exchanger etc. - Google Patents
Method for adjustment of the heat generating process in a rotary kiln with a heat exchanger etc. Download PDFInfo
- Publication number
- US3659829A US3659829A US75836A US3659829DA US3659829A US 3659829 A US3659829 A US 3659829A US 75836 A US75836 A US 75836A US 3659829D A US3659829D A US 3659829DA US 3659829 A US3659829 A US 3659829A
- Authority
- US
- United States
- Prior art keywords
- kiln
- raw material
- heater
- rotary kiln
- feed
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B7/00—Rotary-drum furnaces, i.e. horizontal or slightly inclined
- F27B7/20—Details, accessories, or equipment peculiar to rotary-drum furnaces
- F27B7/42—Arrangement of controlling, monitoring, alarm or like devices
Definitions
- a temperature sensing device is placed in the gas outlet of the rotary kiln and control means are pro- [30]
- the present invention relates to apparatus and method of operating kiln systems and in particular to the method for adjusting the uniformity of the heat generating process therein.
- the maintenance of uniformity of heating conditions of the burning aggregate is one of the main requirements of an economical operation and of the ability to obtain high quality products.
- the equilibrium between heat supply and the amount of raw material is generally achieved by the adjustment of the fuel supply based on measured temperature of the material in the burning zone or by determining the quality of the product at the output end of the kiln.
- the major drawback of this method is the frequent variations of the performance of the heating unit according to the instantaneous conditions and its slowness of response, for instance due to variations in supply of raw material. As the performance varies from any predetermined optimum, nonuniformity of the heating process result in an unfavorable efficiency and quality of production.
- a further drawback is that the relatively complicated combustion process initially adjusted to optimum condition, is altered by variations in regulation of the fuel supply and a number of other conditions, as for instance the supply of combustion air, the shape of the flame and similar factors which must be adjusted.
- the time interval between the origin of the deviation in the supply of raw material into the rotary kiln and the time this deviation is determined in the burning zone is proportional to the speed of advance of the material in the rotary kiln and is therefore relatively long.
- the delay between the origin of the deviation and the moment of any possible interference of compensation for the buring process is therefore relatively large, greatly contributing to an unfavorable influence on the uniformity of the performance.
- the amount of raw material supplied to the rotary kiln is adjusted in response to variations in the temperature of the gases at their outlet from the kiln with respect to a predefined optimum temperature.
- the combustion process is continuously balanced so that the outgoing gas is maintained at as near to possible constant level and with minimum variations of temperature.
- thermometer or other gaseous heat sensing device is inserted at the material inlet end of the kiln (equivalent to the outlets for gases exiting therefrom) and the temperature of the effluent gases are measured.
- the thermometer is connected to a suitable control mechanism, or transducer where the sensed temperature is converted into a signal for directly controlling the feed of the raw material to the intake of the heat exchanger.
- a rotary kiln 10 is supported at each of its ends to rotate about its longitudinal axis.
- a pre-heater for the raw material such as a vertical heat exchanger 12 is mounted adjacent to the entry end of the kiln l0 and is connected therewith with a delivery conduit 14.
- the heat exchanger 12 has a inlet open 16 connected to screw feed mechanism 18 which is driven by motor 20.
- the arrangement shown is purely schematic and is intended merely to be illustrative of the types of arrangements possible for kiln and heat exchangers. Both units as well as the feed mechanism 18 are conventional in nature, and operate in the well known manner.
- the kiln and exchanger may be set at other angles relative to each other or to the ground.
- Other conventional auxilliary apparatus such as heaters, conveyors, etc. are provided.
- material fed through the feed means 18 is preheated in the exchanger 12 and delivered for final treatment through conduct 14 to the oven.
- the gases developed in the oven flow in the counter or reverse direction out of the delivery conduct 14 through the heat exchanger 12 and then out of an exhaust 22.
- the temperature of the outgoing gases from the kiln is sensed by placing a sensor such as thermometer 24 at the gas outlet or material inlet of the kiln.
- the thermometer 24 is connected to a suitable control 26 mechanism such as a transducer or other converter for changing the sensed thermal condition into a suitable electrical or mechanical signal.
- the converted signal is fed directly to the motor 20 which controls the feed mechanism 18 feeding the raw material to the pre-heater or heat exchanger.
- the control mechanism includes suitable circuitry, in addition to the transducer, for providing a signal sufficient to continuously control the rate of feed, and infact, to initiate or discontinue feed if necessary.
- Relays, transformers and other equipment may also be provided in the control means to regulate auxilliary parts or units of the system such as the fuel and air supply for combustion.
- thermometer is placed at the center of the technological operation where variation in temperature is most senstive and most responsive. Unlike the known processes, it is therefore more rapidly responsive to the actual variations and fluctions in the heat conditions within the oven, as it may be effected by all factors. Sensing is thus independent of any one factor such as the condition of the heat exchanger, moisture of the raw material, the final product, or supply of fuel. In general however, the thermometer is capable of sensing a synthesis of the variable factors by being at the center and cross roads of the gas flow and most important at the point which is most sensitive to any disproportionate heat condition which is likely to occur (i.e.; the rotary kiln where the maximum part of the endothermic reaction takes place).
- the control mechanism is preferably provided with a regualting circuit which is operable not only to control the rate of feed but to disconnect the feed entirely in the event of a complete breakdown of the combustion process.
- the circuit may contain means for disconnecting the fuel supply (not shown) to heat the kiln and even the rotation of the kiln if desired as well as the feed of raw material thereto, in the same event.
- a uniform burning process with an optimum output of the whole arrangement is thus achieved with a higher mean output for a given time unit, lower production costs and better quality of the product.
- the major heat consumption is in the rotary kiln and the speed of advance of the gases is high, the time delay between the origin of the disturbance of the process and its determination is very small, so that this method enables a prompt and quick interference and compensatory action into the heat process just at the start of some deviation from normal conditions.
- the required adjustments of the process are simpler and easy to survey as only a single value has to be obtained and a simgle factor (raw material feed) changed in order to achieve a correct and uniform burning.
- the present process also enables simple means to be employed for performance of this change which can be easily surveyed.
- the regulating circuit comprising the thermometer and control mechanism, maintaining constant conditions for a correct burning of the fuel, can be disconnected through the use of appropriate circuit means.
- the method of controlling the uniformity of the heat generating process in kiln apparatus having a feed mechanism for supplying raw material, a pre-heater, and a rotary kiln arranged in tandem with each other, said material passing through said pre-heater into said kiln and effluent combustion gases passing in a counter flow from said kiln into said preheater, comprising the steps of sensing the temperature of the gas effluent from said kiln, and controlling the feed of said raw material to said kiln at the point between said rotary kiln and said pre-heater when the combustion gases exit and the raw material enters the kiln in response to variations in said sensed temperature from a predetrrnined level.
- Apparatus for controlling the combustion process of kilns having a feed mechanism for raw material, a pre-heater and a rotary kiln arranged in tandem with each other, said material passing from said pre-heater into said rotary kiln and the gases of combustion counter-flowing from said kiln into said preheater, comprising a temperature sensing device located at the point of gas outlet and material inlet of said rotary kiln, and means responsive to said sensing device for controlling the feed mechanism to regulate the feeding of said raw material to said kiln with respect to said variations in the temperature of the gas sensed.
- thermomter mounted at the feed inlet to said rotary kiln
- control means comprises a circuit including a transducer and signal generating means for operating said feed mechanism to regulate the rate of flow of said feed.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Muffle Furnaces And Rotary Kilns (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
A rotary kiln system employing a pre-heater for feeding material to the kiln. A temperature sensing device is placed in the gas outlet of the rotary kiln and control means are provided to regulate the rate of feed of raw material to the pre-heater in response to variations in sensed temperature from a predetermined level.
Description
O United States Patent [151 3,659,829 Pos isil et al. Ma 2 1972 [54] METHOD FOR ADJUSTMENT OF THE 5 1 Int. Cl ..F27b 7/02 HEAT GENERATING PROCESS IN A [58] Field of Search ..263/32, 33; 236/15 B ROTARY KILN WITH A HEAT EXCH ANGER ETC [56] References Cited [72] Inventors: Jaroslav Pospisil; Josef Plsek, both of UNITED STATES PATENTS Dvorakova, Czechoslovakia 3,306,237 2/1967 Ransom, Jr. ..263/32 X [73] Assignee: Prerovske strojirny, narodni podnik, 2273l26 2/1942 W B Prerov Czechoslovakia 3,042,388 7/1962 Samty ..263/32 [22] Filed: Sept. 28, 1970 Primary Examiner-John .l. Camby pp No 75 836 Att0rneyRichard Low and Murray Schaffer Related U.S. Application Data 1 ABSTRACT [63] Continuation-impart of Ser. No. 810,844, Mar. 26, A rotary kiln System employing a Pre-heater for feeding 1969, abandoned material to the kiln. A temperature sensing device is placed in the gas outlet of the rotary kiln and control means are pro- [30] Foreign Appncafion priority Data vided to regulate the rate of feed of raw material to the preheater in response to variations in sensed temperature from a Mar. 27, 1968 Czechoslovakia ..2370-68 predetermined leveL [52] U.S. Cl ..263/32 4 Claims, 1 Drawing Figure Patented May 2, 1972 maosuw POSPISIL JoSEP SE'K INVENTORS BACKGROUND OF INVENTION The present invention relates to apparatus and method of operating kiln systems and in particular to the method for adjusting the uniformity of the heat generating process therein.
The use of rotary kilns for the treatment of granular, or fine grain material such as limestone, sand and other aggregate raw material as for cement production and the like is well known. Conventionally such kilns are preceded by a pre-treating heat exchanger through which the raw material is fed. During the course of burning the aggregate an endothermic reaction, at high temperature, take place within the kiln which varies with changes in the nature of the raw material the kiln conditions, the heat supply and other factors.
The maintenance of uniformity of heating conditions of the burning aggregate is one of the main requirements of an economical operation and of the ability to obtain high quality products. In actual practice the equilibrium between heat supply and the amount of raw material is generally achieved by the adjustment of the fuel supply based on measured temperature of the material in the burning zone or by determining the quality of the product at the output end of the kiln. The major drawback of this method is the frequent variations of the performance of the heating unit according to the instantaneous conditions and its slowness of response, for instance due to variations in supply of raw material. As the performance varies from any predetermined optimum, nonuniformity of the heating process result in an unfavorable efficiency and quality of production. A further drawback is that the relatively complicated combustion process initially adjusted to optimum condition, is altered by variations in regulation of the fuel supply and a number of other conditions, as for instance the supply of combustion air, the shape of the flame and similar factors which must be adjusted.
The time interval between the origin of the deviation in the supply of raw material into the rotary kiln and the time this deviation is determined in the burning zone, is proportional to the speed of advance of the material in the rotary kiln and is therefore relatively long. The delay between the origin of the deviation and the moment of any possible interference of compensation for the buring process is therefore relatively large, greatly contributing to an unfavorable influence on the uniformity of the performance.
This object as well as others will be found in the following disclosure.
SUMMARY OF INVENTION In accordance with the present invention the amount of raw material supplied to the rotary kiln is adjusted in response to variations in the temperature of the gases at their outlet from the kiln with respect to a predefined optimum temperature. By making this adjustment the combustion process is continuously balanced so that the outgoing gas is maintained at as near to possible constant level and with minimum variations of temperature. An efficient supply of raw material and the maintenance of all values related to the burning process on a constant level is thus achieved.
In carrying out the present invention a thermometer or other gaseous heat sensing device is inserted at the material inlet end of the kiln (equivalent to the outlets for gases exiting therefrom) and the temperature of the effluent gases are measured. The thermometer is connected to a suitable control mechanism, or transducer where the sensed temperature is converted into a signal for directly controlling the feed of the raw material to the intake of the heat exchanger.
As a result of such an arrangement variations in temperature of the kiln are measured at the most effective and sensitive position, at the place where the incoming feed and the dried raw material efiluent cross.
Full details together with further explanation of the advantages of the present invention follow herein.
BRIEF DESCRIPTION OF DRAWING The attached drawing is a schematic view of drying apparatus which is adapted to the present method and which illustrates its operation.
DESCRIPTION OF INVENTION The drawing and the following description are kept brief, avoiding recitation of well known structures and details of kilns, or heating apparatus structures. Those skilled in this art will readibly have available to them from the prior literature and their knowledge those details omitted here.
As seen in the figure, a rotary kiln 10 is supported at each of its ends to rotate about its longitudinal axis. A pre-heater for the raw material such as a vertical heat exchanger 12 is mounted adjacent to the entry end of the kiln l0 and is connected therewith with a delivery conduit 14. The heat exchanger 12 has a inlet open 16 connected to screw feed mechanism 18 which is driven by motor 20. The arrangement shown is purely schematic and is intended merely to be illustrative of the types of arrangements possible for kiln and heat exchangers. Both units as well as the feed mechanism 18 are conventional in nature, and operate in the well known manner. The kiln and exchanger may be set at other angles relative to each other or to the ground. Other conventional auxilliary apparatus such as heaters, conveyors, etc. are provided.
Briefly, material fed through the feed means 18 is preheated in the exchanger 12 and delivered for final treatment through conduct 14 to the oven. The gases developed in the oven flow in the counter or reverse direction out of the delivery conduct 14 through the heat exchanger 12 and then out of an exhaust 22.
According to the present invention the temperature of the outgoing gases from the kiln is sensed by placing a sensor such as thermometer 24 at the gas outlet or material inlet of the kiln. The thermometer 24 is connected to a suitable control 26 mechanism such as a transducer or other converter for changing the sensed thermal condition into a suitable electrical or mechanical signal. The converted signal is fed directly to the motor 20 which controls the feed mechanism 18 feeding the raw material to the pre-heater or heat exchanger.
The control mechanism includes suitable circuitry, in addition to the transducer, for providing a signal sufficient to continuously control the rate of feed, and infact, to initiate or discontinue feed if necessary. Relays, transformers and other equipment may also be provided in the control means to regulate auxilliary parts or units of the system such as the fuel and air supply for combustion.
The thermometer is placed at the center of the technological operation where variation in temperature is most senstive and most responsive. Unlike the known processes, it is therefore more rapidly responsive to the actual variations and fluctions in the heat conditions within the oven, as it may be effected by all factors. Sensing is thus independent of any one factor such as the condition of the heat exchanger, moisture of the raw material, the final product, or supply of fuel. In general however, the thermometer is capable of sensing a synthesis of the variable factors by being at the center and cross roads of the gas flow and most important at the point which is most sensitive to any disproportionate heat condition which is likely to occur (i.e.; the rotary kiln where the maximum part of the endothermic reaction takes place).
In response to the sensed thermal signal material at an increased or decreased rate, or even at more or less quantity, is fed to the system through the heat exchanger to thereby bring the heat condition back to the predetermined balance and maintain uniformity of the heat generation process. The maintenance of uniformity in the heat generating process can be made without variation in the fuel supply, or other factors, more difficult to control than the material feed. These other factors may therefore be maintained easily at almost contant levels.
The control mechanism is preferably provided with a regualting circuit which is operable not only to control the rate of feed but to disconnect the feed entirely in the event of a complete breakdown of the combustion process. Also the circuit may contain means for disconnecting the fuel supply (not shown) to heat the kiln and even the rotation of the kiln if desired as well as the feed of raw material thereto, in the same event. This is an advantageous derivative of the present invention since the sensing thermometer will rapidly sense any breakdown in the effluent gas long before the same breakdown can be sensed by more conventional methods and the immediate control or shut down of the kiln can be effected be fore the source of heat can do damage.
A uniform burning process with an optimum output of the whole arrangement is thus achieved with a higher mean output for a given time unit, lower production costs and better quality of the product. As the major heat consumption is in the rotary kiln and the speed of advance of the gases is high, the time delay between the origin of the disturbance of the process and its determination is very small, so that this method enables a prompt and quick interference and compensatory action into the heat process just at the start of some deviation from normal conditions. In addition the required adjustments of the process are simpler and easy to survey as only a single value has to be obtained and a simgle factor (raw material feed) changed in order to achieve a correct and uniform burning. The present process also enables simple means to be employed for performance of this change which can be easily surveyed.
In case of some failure of the burning process, the regulating circuit comprising the thermometer and control mechanism, maintaining constant conditions for a correct burning of the fuel, can be disconnected through the use of appropriate circuit means.
It will thus be seen that by the simple arrangement and process herein disclosed a highly advantageous operation of granular heating apparatus is obtained. It will be obvious to those skilled this art, that various modifications and changes may be made depending of the exact type of kiln, heat exchange or feed system used. Accordingly the present disclosure is intended to be illustrative only.
What is claimed is:
1. The method of controlling the uniformity of the heat generating process in kiln apparatus having a feed mechanism for supplying raw material, a pre-heater, and a rotary kiln arranged in tandem with each other, said material passing through said pre-heater into said kiln and effluent combustion gases passing in a counter flow from said kiln into said preheater, comprising the steps of sensing the temperature of the gas effluent from said kiln, and controlling the feed of said raw material to said kiln at the point between said rotary kiln and said pre-heater when the combustion gases exit and the raw material enters the kiln in response to variations in said sensed temperature from a predetrrnined level.
2. The method according to claim 1 wherein the temperature of said effluent gas is continuously sensed and the rate of feed of said raw material is continuously controlled.
3. Apparatus for controlling the combustion process of kilns having a feed mechanism for raw material, a pre-heater and a rotary kiln arranged in tandem with each other, said material passing from said pre-heater into said rotary kiln and the gases of combustion counter-flowing from said kiln into said preheater, comprising a temperature sensing device located at the point of gas outlet and material inlet of said rotary kiln, and means responsive to said sensing device for controlling the feed mechanism to regulate the feeding of said raw material to said kiln with respect to said variations in the temperature of the gas sensed.
4. The apparatus according to claim 3 wherein said temperature sensing means comprises a thermomter mounted at the feed inlet to said rotary kiln, and said control means comprises a circuit including a transducer and signal generating means for operating said feed mechanism to regulate the rate of flow of said feed.
Claims (4)
1. The method of controlling the uniformity of the heat generating process in kiln apparatus having a feed mechanism for supplying raw material, a pre-heater, and a rotary kiln arranged in tandem with each other, said material passing through said pre-heater into said kiln and effluent combustion gases passing in a counter flow from said kiln into said pre-heater, comprising the steps of sensing the temperature of the gas effluent from said kiln, and controlling the feEd of said raw material to said kiln at the point between said rotary kiln and said pre-heater when the combustion gases exit and the raw material enters the kiln in response to variations in said sensed temperature from a predetrmined level.
2. The method according to claim 1 wherein the temperature of said effluent gas is continuously sensed and the rate of feed of said raw material is continuously controlled.
3. Apparatus for controlling the combustion process of kilns having a feed mechanism for raw material, a pre-heater and a rotary kiln arranged in tandem with each other, said material passing from said pre-heater into said rotary kiln and the gases of combustion counter-flowing from said kiln into said pre-heater, comprising a temperature sensing device located at the point of gas outlet and material inlet of said rotary kiln, and means responsive to said sensing device for controlling the feed mechanism to regulate the feeding of said raw material to said kiln with respect to said variations in the temperature of the gas sensed.
4. The apparatus according to claim 3 wherein said temperature sensing means comprises a thermomter mounted at the feed inlet to said rotary kiln, and said control means comprises a circuit including a transducer and signal generating means for operating said feed mechanism to regulate the rate of flow of said feed.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS237068 | 1968-03-27 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3659829A true US3659829A (en) | 1972-05-02 |
Family
ID=5360640
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US75836A Expired - Lifetime US3659829A (en) | 1968-03-27 | 1970-09-28 | Method for adjustment of the heat generating process in a rotary kiln with a heat exchanger etc. |
Country Status (3)
| Country | Link |
|---|---|
| US (1) | US3659829A (en) |
| CA (1) | CA942496A (en) |
| DE (1) | DE1915225A1 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2521667A1 (en) * | 1974-05-15 | 1975-11-27 | Japan Gasoline | METHOD AND DEVICE FOR REGENERATING ACTIVATED CHARCOAL |
| US3942944A (en) * | 1973-03-16 | 1976-03-09 | H. Nielsen & Son Maskinfabrik A/S | Heating of aggregate material for asphalt mixing |
| US20140147799A1 (en) * | 2012-11-23 | 2014-05-29 | John M. Peterman | Metal kiln temperature control system and method |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2273126A (en) * | 1939-08-10 | 1942-02-17 | Brown Instr Co | Control system |
| US3042388A (en) * | 1957-12-17 | 1962-07-03 | Structural Concrete Components | Manufacture of aggregate suitable for use in concrete and like composite materials |
| US3306237A (en) * | 1964-01-28 | 1967-02-28 | Jr George E Ransom | Rotary incinerator and method of operating same |
-
1969
- 1969-03-25 CA CA046,784A patent/CA942496A/en not_active Expired
- 1969-03-26 DE DE19691915225 patent/DE1915225A1/en active Pending
-
1970
- 1970-09-28 US US75836A patent/US3659829A/en not_active Expired - Lifetime
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2273126A (en) * | 1939-08-10 | 1942-02-17 | Brown Instr Co | Control system |
| US3042388A (en) * | 1957-12-17 | 1962-07-03 | Structural Concrete Components | Manufacture of aggregate suitable for use in concrete and like composite materials |
| US3306237A (en) * | 1964-01-28 | 1967-02-28 | Jr George E Ransom | Rotary incinerator and method of operating same |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3942944A (en) * | 1973-03-16 | 1976-03-09 | H. Nielsen & Son Maskinfabrik A/S | Heating of aggregate material for asphalt mixing |
| DE2521667A1 (en) * | 1974-05-15 | 1975-11-27 | Japan Gasoline | METHOD AND DEVICE FOR REGENERATING ACTIVATED CHARCOAL |
| US4008994A (en) * | 1974-05-15 | 1977-02-22 | Japan Gasoline Co., Ltd. | Apparatus and method for regeneration of spent wet active carbon |
| US20140147799A1 (en) * | 2012-11-23 | 2014-05-29 | John M. Peterman | Metal kiln temperature control system and method |
| US9360253B2 (en) * | 2012-11-23 | 2016-06-07 | Gillespie + Powers, Inc | Metal kiln temperature control system and method |
Also Published As
| Publication number | Publication date |
|---|---|
| DE1915225A1 (en) | 1970-08-27 |
| CA942496A (en) | 1974-02-26 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4368678A (en) | Injection of pulverized material into a pressurized furnace | |
| US3659829A (en) | Method for adjustment of the heat generating process in a rotary kiln with a heat exchanger etc. | |
| US3519254A (en) | Method and apparatus for the control of burner heat distribution | |
| US4402462A (en) | Process for controlling a grinding installation | |
| US3091443A (en) | Kiln automatic control method and apparatus | |
| US3204341A (en) | Process and apparatus for drying wet particulate material to a desired moisture content | |
| US3627287A (en) | Rotary kiln control apparatus and programming | |
| US4557057A (en) | Apparatus for the drying of tobacco materials | |
| CS195669B2 (en) | Method of regulating incinerators for heat treating fine-grained materials | |
| KR100419768B1 (en) | Method and apparatus for controlling a crusher of a pulverized coal injection | |
| US3483363A (en) | Method and apparatus for maximizing the output of a rotary kiln | |
| US2403976A (en) | System of pulverizing, feeding, and transporting of material | |
| US2484539A (en) | Means for rotary kiln temperature control | |
| CS215079B2 (en) | Method of regulation of the relation of the quantity of fine grained material and furnace waste gases | |
| SU483659A1 (en) | Moisture Control Device for Bulk Materials | |
| SU985685A1 (en) | Method of automatic control of roasting process of raw mixture in rotating furnace | |
| SU972207A1 (en) | Method for automatically controlling thermal conditions of rotary kilns | |
| SU456129A1 (en) | The method of automatic control of the firing process in fluidized bed furnaces | |
| SU365383A1 (en) | METHOD OF AUTOMATIC REGULATION OF THE QUALITY OF BONDING OF ANGLOMERATION CHARGE | |
| SU857074A1 (en) | Method of automatic control of ceramic article annealing process in slot furnace | |
| SU476239A1 (en) | AUTOMATIC REGULATION METHODS ARE AUTOMATIC (Regular and i: ipouecca Ozhig) • Kliiker in the furnace: x dry cement production with direct combustion: • heat exchanger with: • dry-heat cement production with direct burner: 1 heat exchanger with kiln: heat exchanger.mi, and can be used: P'Olsazano> &! a ;; edpri ;; x cement and lamelleisti. A method is known for automatically adjusting the process of clinker from the furnace with indirect heat exchangers by the process, including after the fourth heat exchange stage, measured The costs and changes in the supply of the raw material mixture and fuel, the measurement of the temperature of the neiphera air supplied to the bed and representing the mixture of hot and cold air, the measurement of the temperature of exhaust gases of the first and third stages of heat exchange. This is because the temperature of the primary air stabilizes. One: it does not remain constant during the operation process. When this temperature fluctuates, the stability of the temneururized floor in the furnace and in the heat exchangers is disturbed, as a result of which decreases' K clinker quality. The purpose of the invention is to reduce fuel consumption for firing and improve the quality of the locker. To do this additionally! {31 measure the difference. between the signal proportional to the temperature of the waste gases and sypnal, pro:;: the value of the active current] of the 1 drive of the peppi si difference of 5 between the signal, P | p01U | rational temperature of the exhaust gases of the first stage of heat exchange and the signal.m proportional to the flow rate, the value of which!: is used to change, feed fuel with a correction of 10 largest active flash drive pschn ''.! Rich supply of raw !! mixtures regulate iio faults between the c; 1gpal, proportional to the temperature of the waste gas signal proportional to the consumption of the raw material estimate, and the flow of cold air is controlled by the temperature nopBimiioro of the air. The invention globally removed the drawing. Chu 2 hot primary air, supply of cold air 3 and supply of - / aspration air, exit 5 of exhaust gas, feed 6 of raw mix, heat exchangers 7, S, 9, 10, first, second, third and Thu-25 iBepToii heat exchange stools, rotating us kiln //, grate cooler 12, actuator oven 13, regulator 14 to change the air of the aspratation air, regulator / 5 to change the flow of cold air, regulator | |
| SU1232285A1 (en) | Apparatus for control system for regulating heat conditions of ball aerated mill | |
| SU1435633A1 (en) | Method of controlling the process of heat treatment of phosphorite pellets | |
| JPS61183126A (en) | Combustion controlling apparatus for glass melting furnace | |
| SU803974A1 (en) | Method of automatic control of crushing unit of raw material mill, rotary furnace and cement mill |