CA1239153A - Method and apparatus for producing cement clinker including white cement - Google Patents
Method and apparatus for producing cement clinker including white cementInfo
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- CA1239153A CA1239153A CA000498780A CA498780A CA1239153A CA 1239153 A CA1239153 A CA 1239153A CA 000498780 A CA000498780 A CA 000498780A CA 498780 A CA498780 A CA 498780A CA 1239153 A CA1239153 A CA 1239153A
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- cement
- nodules
- fluidized bed
- cement clinker
- producing
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Abstract
Abstract of Disclosure A method and apparatus for producing cement which includes intermixing the cement forming raw materials with water, coal or coke and cement as a binder and foaming this mixture of materials into nodules by pelletizing or extrusion. The system is particularly designed for use in making white cement where raw marerials low in coloring compound are used as raw feed.
The nodules are then sized to obtain a feed material having a size range on the order of one quarter inch by 14 mesh which is suitable for use in a fluidized bed reactor. The nodulized raw material is thermally processed in a fluidized bed reactor at temperatures in the range of approximately 2500° to 2700°F for white cement and 2350° - 2450°F for typical gray Portland Cement. The coal or coke mixed with the raw material serves to supply between 60% and 90% percent of the fuel required for the process with the remainder being supplied directly to the fluidized bed. This fuel serves to provide internal reduction conditions within the particles of material. The product is discharged from a fluidized bed and cooled in an indirect heat exchanger.
The nodules are then sized to obtain a feed material having a size range on the order of one quarter inch by 14 mesh which is suitable for use in a fluidized bed reactor. The nodulized raw material is thermally processed in a fluidized bed reactor at temperatures in the range of approximately 2500° to 2700°F for white cement and 2350° - 2450°F for typical gray Portland Cement. The coal or coke mixed with the raw material serves to supply between 60% and 90% percent of the fuel required for the process with the remainder being supplied directly to the fluidized bed. This fuel serves to provide internal reduction conditions within the particles of material. The product is discharged from a fluidized bed and cooled in an indirect heat exchanger.
Description
~L,r~3~3~.5 METHOD AND APPARATUS FOX PRODUCING CEMENT CLINKER
INCLUDING WHITE CEMENT
Background of the Invention This invention relates to a process and apparatus for the production of cement clinker and in particular to a process and apparatus for the manufacture of cement clinker utilizing a fluidized bed apparatus. The prows and apparatus are particularly suited to small capacity plants and specifically to the production of cement of a light color or white cement.
Prick to the resent invention, port land cement has been produced in long rotary kilns utilizing the wet or dry processes, relatively short kilns utilizing suspension preheater, with or without precalcining systems, and in fluidized bed reactors. Most modern cement plants are designed to produce large capacities on the order of 1,000 tons per day and up to 5,000 ton per day. There ace many situation where it is desirable to provide a cement clinker producing facility having a small capacity on the order of between 25 tons pew day and 500 tons per day. These small capacity plants are sometimes referred to a "mini" cement elands.
Prior to the present invention, "mini" cement plants have utilized small rotary kilns with perhaps a single stage preheater and a rotary cooler. To my knowledge, a small capacity cement clinker production facility utilizing a fluidized bed apparatus and auxiliary equipment according to the prevent invention has no been proposed.
An efficient low capacity cement plant is desirable where cement usage is low such as in remote regions of developing countries and for the manufacture of specialty cements such a white cement .,.
39~4L/ml~-3 -1-39~!L53 White cement it produced from raw material low in coloring elements such a iron, manganese and chromium, normally utilizing high grade limestone, white clay and pure silica as raw materials. White cement it used primarily for a~chitectual applications requiring white or colored concrete.
Due to a low iron content, normally less than 0.5~
Foe, the potential liquid formation within the clinkering process for white cement is low and the burn ability of the raw material it very hard. A typical silica modules foe white clinker is in the 4 to 6 Lange compared with 2.3 and 3~0 for gray cement. As is well known the silica modules is determined as follows:
Silica Modulus Aye I Foe Due to the difficult burn ability of the raw materials, the raw materials for white cement manufacture are usually ground very fine with 90% to US being -200 mesh being a typical grind. The grinding takes place in raw mills utilizing ceramic or alloy steel grinding media to reduce possible iron contamination ox the raw material.
With white cement manufacturing apparatus, recuperative air quenching clinker coolers used in normal gray cement applications are not utilized as the clinker must be protected against oxidation of the iron content contained therein down to at least 700C and procurable tower. Typically, water and oil sprays era used at the discharge end of the kiln to prevent oxidation after the burning zone end water quenching in drag conveyors is used after the clinker it discharged from the kiln. Rome application haze used a decolonizing cooler using 3944L/mlr-3 -2-,.,,_~
~23~L53 a Coy or CO gas as the cooling medium. The absence of a recuperative air quenching clinker cooler tends to result in high fuel consumption for a white cement manufacturing process.
Equipment used conventionally foe the production of white cement generally has short refractory life. This is due to the low potential liquid in the raw material which results in little coating in the hot zone of the conventional rotary kiln.
Fuels utilized in thy manufacture of white cement are usually either natural gas or oil. Solid fuels such as coke or coal are not normally used in the manufacture of white cement due to the potential spot contamination of the material caused by ash fusion and incomplete chemical dispersion of the ash.
As stated in U.S. Patent 3,114,648 issued December 17, 1963, free carbon in the clinker is objectionable due to the dark color it imparts to the finished cement.
Due to the difficult burn ability of raw meal used for manufacturing white cement, the lack of a clinker cooler which utilizes heat recuperation and high kiln radiation due to high Jo temper no of the kiln, fuel consumption for manufacturing white cement is typically 50% to 100% greater than that for the manufacture of gray cement clinker. It would be desirable to provide a process and apparatus capable of reducing the fuel consumption required to produce white cement, increase refractory life and permit the utilization of coal as a fuel.
It would also be desirable to provide a cement manufacturing process and apparatus which would allow reduced Cole investment for a low capacity plant and be capable of utilizing solid fuel.
.
Lowe Summary It it an object of this invention to provide a process and apparatus for producing cement clinker which it specifically designed for small capacities.
It is another object of this invention to provide a process for manufacturing white cement clinker which has reduced fuel consumption as compared with known methods log manufacture of such cement.
It is another object of the invention to provide an apparatus for producing light colored cement which is capable of utilizing a solid fuel such as coal or coke in the combustion process.
further object of this invention to provide a method and apparatus for manufacturing cement at small capacities which increases equipment.
In general, the foregoing and other objects will be carried out by providing a process of producing white cement comprising the steps ox providing cement-forming raw materials low in coloring elements; intermixing water, carbon beating material and a binder with the cement forming raw materials to form a mixture; forming the mixture into nodules; drying the nodules;
sizing the nodules to obtain a feed material having a particle size within a selected size range; supplying the feed material to a vessel; passing air upwardly through the material within the vessel to maintain a fluidized bed of material within the vessel; thermal processing the feed material within the fluidized bed by combustion of the carbon bearing material within the feed material and supplying additional fuel to the fluidized bed for maintaining the fluidized bed at a temper go in the range of approximately Tao 2700 for 3944L/ml~-3 I
Jo white cement and Tao 2450 for gray cement; discharging cement clinker from the fluidized bed by displacement; and cooling the discharged material.
With the present invention, a feed preparation system for producing white cement include mixing finely ground raw materials low in coloring element with water, coal or coke and white cement as a binder to form a mixture. If the process and apparatus are used to produce grew or ordinary port land cement, the raw material can be normal cement raw meal and the binder can be ordinary Port land cement. The mixture is conveyed to either a disc ~elletizer or an extrude to produce the nodules. The nodules are then dyed in a tray dryer and may be stored after drying. The nodule produced by the extrusion process are then crushed and screened to produce a feed material of a desired it range. The disc pelletizer nodules in most cases will be used directly after drying. The sized feed material is then supplied to a fluidized bed reactor for thermal processing to produce cement clinker. An indirect heat exchange is used to recuperate some of the heat of the discharged product and use such heat for drying the material.
The hot spent fluidizing gases from the reactor Aye used to preheat fluidi~irlg gas and air or combustion by means of an indirect heat exchanger.
Brief Description of the Drawings The invention will be described in connection with the annexed drawings wherein:
Fig. 1 is a diagrammatic view of the apart of the punt inYen~ion;
3944L/mlr-3 I
I. f . , A= --~L~3~153 Fig. 2 it a diagrammatic view a portion of a modified apparatus for carrying out the process of the prevent invention; and Fig. 3 it a diagrammatic view on an enlarged scale of the pyroprocessing portion of apprise utilized for carrying out the process of the present invention.
Description of the Preferred Environment With the resent invention, cHmHnt forming raw materials are metered prom a bin such as that illustrated at 5 in Fig. l lo onto a belt conveyer 6. If the process and apparatus is to be utilized for manufacturing white cement, the raw materials must be low in coloring elements, that is low in iron, manganese and chromium. Carbon bearing materials such as coal or coke is added to the belt 6 from a bin 7 in an amount sufficient to bring the carbon content of the final raw material to the range of approximately 5% to I by weight carbon content. This may be between 60% and 80% of the process fuel requirements but up to 90~ ox the required fuel to obtain clinkering temperatures can be added with the pellet feed. A suitable binder, preferably cement is added from a bin 8 to the conveyor 6 in an amount of up to 5% by weight. If white cement is being produced, the binder should be white cement. The apparatus may include additional bins such as that indicated at 9 for recycled material and a spare bin 10 which may be used for an additive if required by the process.
The raw material, the coal or coke and binder are transported by conveyor 6 to apparatus for combining the solid material with water and forming the mixture of water, raw material, coal or coke and cement into nodules. In Fig. l, 3 _~_ so this apparatus it illustrated as a pug mill 15 and extrude 16. The pug mill 15 ~ixe6 and conveys the material to an extrude 16 where extrusions or nodules are formed. The extruded material it then supplied to a tray dryer generally indicated at I The dryer is supplied with heated drying gas Tao conduit lg. Exhaust gas from the dryer is supplied through a conduit 20 and fan 21 to a high efficiency dust kilter 22. Dust from the collector 22 is removed at 23 and may be supplied to the recycle bin 9. Rudy nodules are then sized to obtain a feed material having a selected size range.
In the embodiment illustrated in Fig. 1, sizing of the nodules or extrusion is carried out by supplying the nodules to a roll crusher 25. Crushed material then goes through a series of screens generally indicated at 26 where a desired sized material is removed at 27 and supplied as feed material to a bucket elevator 28. Oversized material is taken off at 29 for recycle to the roll crusher 25. Undersized material is removed at 30 log recycle to bin 9. In the referred form, the material is sized to produce a product having a size range of one-fourth inch by 14 mesh.
The conveyor 6, pug mill 15, extrude 16, tray dryer 18, crusher 25 and screen system 26 together constitute a feed preparation system generally indicated at 12. The conveyor, pug mill and extrude define means for combining the cement forming raw materials with carbon bearing material, a binder and water to form a mixture and for forming the mixture into nodules. The tray dryer and hot gas inlet 19 define a mean for drying the nodules.
In the preferred method, the extrusions are dyed on tray dryer I to produced a hard nodule discharged at 24. The dyed nodules are sent to storage fox a period of 1 to 3 days for wow 7_ ~39~L53 aging to allow the binder to increase the pellet or nodule strength. The tweezed or age pellets may then be supplied to the roll crusher 25 rather than directly from discharge as illustrated.
An alternate weed preparation system it illustrated in Fig.
INCLUDING WHITE CEMENT
Background of the Invention This invention relates to a process and apparatus for the production of cement clinker and in particular to a process and apparatus for the manufacture of cement clinker utilizing a fluidized bed apparatus. The prows and apparatus are particularly suited to small capacity plants and specifically to the production of cement of a light color or white cement.
Prick to the resent invention, port land cement has been produced in long rotary kilns utilizing the wet or dry processes, relatively short kilns utilizing suspension preheater, with or without precalcining systems, and in fluidized bed reactors. Most modern cement plants are designed to produce large capacities on the order of 1,000 tons per day and up to 5,000 ton per day. There ace many situation where it is desirable to provide a cement clinker producing facility having a small capacity on the order of between 25 tons pew day and 500 tons per day. These small capacity plants are sometimes referred to a "mini" cement elands.
Prior to the present invention, "mini" cement plants have utilized small rotary kilns with perhaps a single stage preheater and a rotary cooler. To my knowledge, a small capacity cement clinker production facility utilizing a fluidized bed apparatus and auxiliary equipment according to the prevent invention has no been proposed.
An efficient low capacity cement plant is desirable where cement usage is low such as in remote regions of developing countries and for the manufacture of specialty cements such a white cement .,.
39~4L/ml~-3 -1-39~!L53 White cement it produced from raw material low in coloring elements such a iron, manganese and chromium, normally utilizing high grade limestone, white clay and pure silica as raw materials. White cement it used primarily for a~chitectual applications requiring white or colored concrete.
Due to a low iron content, normally less than 0.5~
Foe, the potential liquid formation within the clinkering process for white cement is low and the burn ability of the raw material it very hard. A typical silica modules foe white clinker is in the 4 to 6 Lange compared with 2.3 and 3~0 for gray cement. As is well known the silica modules is determined as follows:
Silica Modulus Aye I Foe Due to the difficult burn ability of the raw materials, the raw materials for white cement manufacture are usually ground very fine with 90% to US being -200 mesh being a typical grind. The grinding takes place in raw mills utilizing ceramic or alloy steel grinding media to reduce possible iron contamination ox the raw material.
With white cement manufacturing apparatus, recuperative air quenching clinker coolers used in normal gray cement applications are not utilized as the clinker must be protected against oxidation of the iron content contained therein down to at least 700C and procurable tower. Typically, water and oil sprays era used at the discharge end of the kiln to prevent oxidation after the burning zone end water quenching in drag conveyors is used after the clinker it discharged from the kiln. Rome application haze used a decolonizing cooler using 3944L/mlr-3 -2-,.,,_~
~23~L53 a Coy or CO gas as the cooling medium. The absence of a recuperative air quenching clinker cooler tends to result in high fuel consumption for a white cement manufacturing process.
Equipment used conventionally foe the production of white cement generally has short refractory life. This is due to the low potential liquid in the raw material which results in little coating in the hot zone of the conventional rotary kiln.
Fuels utilized in thy manufacture of white cement are usually either natural gas or oil. Solid fuels such as coke or coal are not normally used in the manufacture of white cement due to the potential spot contamination of the material caused by ash fusion and incomplete chemical dispersion of the ash.
As stated in U.S. Patent 3,114,648 issued December 17, 1963, free carbon in the clinker is objectionable due to the dark color it imparts to the finished cement.
Due to the difficult burn ability of raw meal used for manufacturing white cement, the lack of a clinker cooler which utilizes heat recuperation and high kiln radiation due to high Jo temper no of the kiln, fuel consumption for manufacturing white cement is typically 50% to 100% greater than that for the manufacture of gray cement clinker. It would be desirable to provide a process and apparatus capable of reducing the fuel consumption required to produce white cement, increase refractory life and permit the utilization of coal as a fuel.
It would also be desirable to provide a cement manufacturing process and apparatus which would allow reduced Cole investment for a low capacity plant and be capable of utilizing solid fuel.
.
Lowe Summary It it an object of this invention to provide a process and apparatus for producing cement clinker which it specifically designed for small capacities.
It is another object of this invention to provide a process for manufacturing white cement clinker which has reduced fuel consumption as compared with known methods log manufacture of such cement.
It is another object of the invention to provide an apparatus for producing light colored cement which is capable of utilizing a solid fuel such as coal or coke in the combustion process.
further object of this invention to provide a method and apparatus for manufacturing cement at small capacities which increases equipment.
In general, the foregoing and other objects will be carried out by providing a process of producing white cement comprising the steps ox providing cement-forming raw materials low in coloring elements; intermixing water, carbon beating material and a binder with the cement forming raw materials to form a mixture; forming the mixture into nodules; drying the nodules;
sizing the nodules to obtain a feed material having a particle size within a selected size range; supplying the feed material to a vessel; passing air upwardly through the material within the vessel to maintain a fluidized bed of material within the vessel; thermal processing the feed material within the fluidized bed by combustion of the carbon bearing material within the feed material and supplying additional fuel to the fluidized bed for maintaining the fluidized bed at a temper go in the range of approximately Tao 2700 for 3944L/ml~-3 I
Jo white cement and Tao 2450 for gray cement; discharging cement clinker from the fluidized bed by displacement; and cooling the discharged material.
With the present invention, a feed preparation system for producing white cement include mixing finely ground raw materials low in coloring element with water, coal or coke and white cement as a binder to form a mixture. If the process and apparatus are used to produce grew or ordinary port land cement, the raw material can be normal cement raw meal and the binder can be ordinary Port land cement. The mixture is conveyed to either a disc ~elletizer or an extrude to produce the nodules. The nodules are then dyed in a tray dryer and may be stored after drying. The nodule produced by the extrusion process are then crushed and screened to produce a feed material of a desired it range. The disc pelletizer nodules in most cases will be used directly after drying. The sized feed material is then supplied to a fluidized bed reactor for thermal processing to produce cement clinker. An indirect heat exchange is used to recuperate some of the heat of the discharged product and use such heat for drying the material.
The hot spent fluidizing gases from the reactor Aye used to preheat fluidi~irlg gas and air or combustion by means of an indirect heat exchanger.
Brief Description of the Drawings The invention will be described in connection with the annexed drawings wherein:
Fig. 1 is a diagrammatic view of the apart of the punt inYen~ion;
3944L/mlr-3 I
I. f . , A= --~L~3~153 Fig. 2 it a diagrammatic view a portion of a modified apparatus for carrying out the process of the prevent invention; and Fig. 3 it a diagrammatic view on an enlarged scale of the pyroprocessing portion of apprise utilized for carrying out the process of the present invention.
Description of the Preferred Environment With the resent invention, cHmHnt forming raw materials are metered prom a bin such as that illustrated at 5 in Fig. l lo onto a belt conveyer 6. If the process and apparatus is to be utilized for manufacturing white cement, the raw materials must be low in coloring elements, that is low in iron, manganese and chromium. Carbon bearing materials such as coal or coke is added to the belt 6 from a bin 7 in an amount sufficient to bring the carbon content of the final raw material to the range of approximately 5% to I by weight carbon content. This may be between 60% and 80% of the process fuel requirements but up to 90~ ox the required fuel to obtain clinkering temperatures can be added with the pellet feed. A suitable binder, preferably cement is added from a bin 8 to the conveyor 6 in an amount of up to 5% by weight. If white cement is being produced, the binder should be white cement. The apparatus may include additional bins such as that indicated at 9 for recycled material and a spare bin 10 which may be used for an additive if required by the process.
The raw material, the coal or coke and binder are transported by conveyor 6 to apparatus for combining the solid material with water and forming the mixture of water, raw material, coal or coke and cement into nodules. In Fig. l, 3 _~_ so this apparatus it illustrated as a pug mill 15 and extrude 16. The pug mill 15 ~ixe6 and conveys the material to an extrude 16 where extrusions or nodules are formed. The extruded material it then supplied to a tray dryer generally indicated at I The dryer is supplied with heated drying gas Tao conduit lg. Exhaust gas from the dryer is supplied through a conduit 20 and fan 21 to a high efficiency dust kilter 22. Dust from the collector 22 is removed at 23 and may be supplied to the recycle bin 9. Rudy nodules are then sized to obtain a feed material having a selected size range.
In the embodiment illustrated in Fig. 1, sizing of the nodules or extrusion is carried out by supplying the nodules to a roll crusher 25. Crushed material then goes through a series of screens generally indicated at 26 where a desired sized material is removed at 27 and supplied as feed material to a bucket elevator 28. Oversized material is taken off at 29 for recycle to the roll crusher 25. Undersized material is removed at 30 log recycle to bin 9. In the referred form, the material is sized to produce a product having a size range of one-fourth inch by 14 mesh.
The conveyor 6, pug mill 15, extrude 16, tray dryer 18, crusher 25 and screen system 26 together constitute a feed preparation system generally indicated at 12. The conveyor, pug mill and extrude define means for combining the cement forming raw materials with carbon bearing material, a binder and water to form a mixture and for forming the mixture into nodules. The tray dryer and hot gas inlet 19 define a mean for drying the nodules.
In the preferred method, the extrusions are dyed on tray dryer I to produced a hard nodule discharged at 24. The dyed nodules are sent to storage fox a period of 1 to 3 days for wow 7_ ~39~L53 aging to allow the binder to increase the pellet or nodule strength. The tweezed or age pellets may then be supplied to the roll crusher 25 rather than directly from discharge as illustrated.
An alternate weed preparation system it illustrated in Fig.
2 and generally indicated at AYE. In this feed preparation system, raw material, carbon and cement are supplied through similar bins 5, 7 and 8 to a common conveyor 6 in the manner of Fig. 1. The conveyor feeds the material to a disk or drum pelletizer 40. Water is added to the disk pelletizer and mixing lakes place directly in the pelletizer with the pelletizer being controlled to produce a nodule or pellet having size range of one quarter inch by 14 mesh. In this embodiment, wet pellets leave the pelletizer 40 and are transported as indicated at 41 to a tray dryer 18. The tray dryer is supplied with heated drying gas at lug and spent drying gas is exhausted through conduit 20, fan 21 and high efficiency dust collector 22 in the manner ox Fig. l. Dust is returned at 23 to bin 9. The discharge from dryer 18 may go to a screen illustrated at 26 with oversize being supplied at 29 to a small crusher (not shown in Fig. 2) and undersized material being returned at 30 to bin 9. Priorly sized feed material it discharged at 27 for further processing. In this embodiment as in Fig. l, it is preferred that the dyed pellet be sent to storage for between one and three days.
As illustr~ed in Fig. l, properly sized material is supplied by bucket elevator 28 to a storage bin I Material is metered out of the bin 45 and conveyed through line 46 to a 1uidized bed reactor generally indicated at 50 for thermal prosing the material to produce cement clinker. Revering to Fig. 3, the fluidized bed reactor 50 includes a vessel 51 394~L~mls-3 -8-having an inlet 52 for the dried and sized material from the feed preparation stem 12 or AYE (Fig. 1 or Fig. 2 ee~pectively). The vessel 50 is divided into an upper material chamber 53 and a lower plenum chamber 54 by means of a gas permeable grid 55 known in the art. Means are provided for supplying air under pressure or fluidizing gas to the plenum chamber 54 for passage upwardly through the grid 55 and a bed 57 of feed material to thereby e6eablish and maintain a fluidized bed 60 of nodules. Fuel in addition to thee combined with the feed material it supplied through nozzle 61 to the bed 64 combustion within the fluidized bed 60. The amount of fuel added is sufficient to maintain the material within the fluidized bed at cement clinkering temperatures.
The air supply of the prevent system is illustrated in Fig.
As illustr~ed in Fig. l, properly sized material is supplied by bucket elevator 28 to a storage bin I Material is metered out of the bin 45 and conveyed through line 46 to a 1uidized bed reactor generally indicated at 50 for thermal prosing the material to produce cement clinker. Revering to Fig. 3, the fluidized bed reactor 50 includes a vessel 51 394~L~mls-3 -8-having an inlet 52 for the dried and sized material from the feed preparation stem 12 or AYE (Fig. 1 or Fig. 2 ee~pectively). The vessel 50 is divided into an upper material chamber 53 and a lower plenum chamber 54 by means of a gas permeable grid 55 known in the art. Means are provided for supplying air under pressure or fluidizing gas to the plenum chamber 54 for passage upwardly through the grid 55 and a bed 57 of feed material to thereby e6eablish and maintain a fluidized bed 60 of nodules. Fuel in addition to thee combined with the feed material it supplied through nozzle 61 to the bed 64 combustion within the fluidized bed 60. The amount of fuel added is sufficient to maintain the material within the fluidized bed at cement clinkering temperatures.
The air supply of the prevent system is illustrated in Fig.
3 and includes a blower 62 having it outlet 63 connected via conduit 64 to an auxiliary air heater 65 or connection through inlet 66 to the plenum chamber 54. The outlet I it also connected to a conduit 68 which is connected to a heat exchanger 70 within a knock-out chamber 71. Heat exchanger 70 is connected via conduit 72 to the air heater chamber 65.
ilk the present invention, carbon present in the feed will supply 60% to 80% of the prosody fuel betides being used for maintaining thermal reduction condition within the feed particles. When manufacturing white cement, this internal reduction condition controls the iron reactions Jo keep from forming Foe which it an undesirable coloring compound.
The reduction aid in the production of a whiter or brighter product by eliminating potential oxidation of the iron convene present in the raw material. While the raw material for white or light colored cement will contain a low iron content as compared with gluey Port land cement, that iron which it prevent 394~L/mlr-3 I
t ~L239~l~3 should be converted to Foe rather than to Foe to avoid the objectionable color. This it done in part by maintaining the reducing conditions internally within the particles. The present invention differs loom that disclosed in U.S. Patent No. 3,114,648 which utilizes fuel sprayed onto elite to keep the fuel in close proximity to the raw meal.
With the present invention, the carbon bearing material is mixed with the raw feed. This mean chat a solid fuel heretofore considered undesirable in the production of white cement may be utilized. The utilization of solid fuel and the corresponding reduction in gas or liquid fuel it particularly advantageous to the production of cement in those parts of the world where coal it more readily available than gas or oil With the present invention, the temperature within the fluidized bed is maintained on the order of 2500 to 2700F
for white cement and between approximately 2350 and 2450 F
fox kiwi cement. This compares with temperatures used in the prior act ox 2700 to 2900 F or the manufacture of white cement. The lower temperature Jill mean a reduced fuel consumption and improved refractory life. The temperature is maintained lot which is necessary to produce the clinker with a free line content of under 2%.
A material is supplied to the fluidized bed 60, product it discharged by displacement through overflow conduit 75 to an indirect cooler 76. Material discharged from vessel 51 it by displacement so that the rate of discharge of material depends upon the rate of feed of material to the vessel. Material retention time should be on the order of 1 to 2 hours Product discharged through conduit 75 is supplied to heat exchanger 76 where it it cooled by indirect heat exchange wit cooling air supplied from a source such as a blower snot shown) 3944L~mlL-3 -10-~L2391 53 through conduit 77 to heat e~changar coil I Air it heated it the heat exchanger 76 and discharged from coil 78 through conduit 79. As illustrated in Fig. 1, conduit 79 it flow connected to conduit 19 80 that the thus heated cooling air is utilized for drying materials in the tray dryer thereby reducing overall fuel consumption of the process. Product it discharged from cooler 76 through outlet 80. Depending upon the raw material and the temperature of bed 60, a product may be either cement clinker or an intermediate product. The use of the indirect heat exchange it required in the production of white cement clinker to prevent the oxidation of the iron compounds which oxidation is hastened at elevated temperatures. If grew cement is being manufactured, it may be desirable to use a direct heat exchanger for heat recovery.
Spend fluidizing gases will entrain a portion of the incoming feed and some fine product. This material will be discharged through an outlet 85 and through a knock-out chamber 71. In the knock-out chamber 71, the elutriated fine incoming feed and fine product will be separated from the gases in which it is entrained. This product will be discharged through a suitable air lock US.
A vent or bleed air system 87 is flow connected to a knock-out chamber it for the purpose of cooling the off guy leaving the reactor so that they may be supplied through conduit 88 to a high efficiency dust collector 89 with the solid material being separated and discharged at 90 and the gas bring discharged to atmosphere through fan 91 and stack 92.
The bleed air serves to protect the bags of a bag type collector.
If desired, cold water coil can be used for the final cooling step of the product in heat exchanger 76.
3944L/mlr-3 I I
It should be noted that air heater 65 may be required to be a separate fired vessel for the purposes of startup For a "mini cement slant, the following approximate issue for reactors on are to be considered:
Clinker Capacity in Reactor Size Tons Per DavDiameter in feet
ilk the present invention, carbon present in the feed will supply 60% to 80% of the prosody fuel betides being used for maintaining thermal reduction condition within the feed particles. When manufacturing white cement, this internal reduction condition controls the iron reactions Jo keep from forming Foe which it an undesirable coloring compound.
The reduction aid in the production of a whiter or brighter product by eliminating potential oxidation of the iron convene present in the raw material. While the raw material for white or light colored cement will contain a low iron content as compared with gluey Port land cement, that iron which it prevent 394~L/mlr-3 I
t ~L239~l~3 should be converted to Foe rather than to Foe to avoid the objectionable color. This it done in part by maintaining the reducing conditions internally within the particles. The present invention differs loom that disclosed in U.S. Patent No. 3,114,648 which utilizes fuel sprayed onto elite to keep the fuel in close proximity to the raw meal.
With the present invention, the carbon bearing material is mixed with the raw feed. This mean chat a solid fuel heretofore considered undesirable in the production of white cement may be utilized. The utilization of solid fuel and the corresponding reduction in gas or liquid fuel it particularly advantageous to the production of cement in those parts of the world where coal it more readily available than gas or oil With the present invention, the temperature within the fluidized bed is maintained on the order of 2500 to 2700F
for white cement and between approximately 2350 and 2450 F
fox kiwi cement. This compares with temperatures used in the prior act ox 2700 to 2900 F or the manufacture of white cement. The lower temperature Jill mean a reduced fuel consumption and improved refractory life. The temperature is maintained lot which is necessary to produce the clinker with a free line content of under 2%.
A material is supplied to the fluidized bed 60, product it discharged by displacement through overflow conduit 75 to an indirect cooler 76. Material discharged from vessel 51 it by displacement so that the rate of discharge of material depends upon the rate of feed of material to the vessel. Material retention time should be on the order of 1 to 2 hours Product discharged through conduit 75 is supplied to heat exchanger 76 where it it cooled by indirect heat exchange wit cooling air supplied from a source such as a blower snot shown) 3944L~mlL-3 -10-~L2391 53 through conduit 77 to heat e~changar coil I Air it heated it the heat exchanger 76 and discharged from coil 78 through conduit 79. As illustrated in Fig. 1, conduit 79 it flow connected to conduit 19 80 that the thus heated cooling air is utilized for drying materials in the tray dryer thereby reducing overall fuel consumption of the process. Product it discharged from cooler 76 through outlet 80. Depending upon the raw material and the temperature of bed 60, a product may be either cement clinker or an intermediate product. The use of the indirect heat exchange it required in the production of white cement clinker to prevent the oxidation of the iron compounds which oxidation is hastened at elevated temperatures. If grew cement is being manufactured, it may be desirable to use a direct heat exchanger for heat recovery.
Spend fluidizing gases will entrain a portion of the incoming feed and some fine product. This material will be discharged through an outlet 85 and through a knock-out chamber 71. In the knock-out chamber 71, the elutriated fine incoming feed and fine product will be separated from the gases in which it is entrained. This product will be discharged through a suitable air lock US.
A vent or bleed air system 87 is flow connected to a knock-out chamber it for the purpose of cooling the off guy leaving the reactor so that they may be supplied through conduit 88 to a high efficiency dust collector 89 with the solid material being separated and discharged at 90 and the gas bring discharged to atmosphere through fan 91 and stack 92.
The bleed air serves to protect the bags of a bag type collector.
If desired, cold water coil can be used for the final cooling step of the product in heat exchanger 76.
3944L/mlr-3 I I
It should be noted that air heater 65 may be required to be a separate fired vessel for the purposes of startup For a "mini cement slant, the following approximate issue for reactors on are to be considered:
Clinker Capacity in Reactor Size Tons Per DavDiameter in feet
4.0 6.0 100 By 200 12.0 300 14.5 500 18.5 From the foregoing it should be apparent that the objects ox the present invention have been carried out. system has been provided log producing white cement which ha reduced fuel consumption as compared with prior apparatus in that the reactions can be carried out at lower temeetatures. An economical system has been provided in that lower capital C06t5 are required with the present invention as compared with the capital costs of a rotary kiln system used by the prior apparatus. This is true for not only the production of white cement, but alto the system as used for producing Port land cement. The utilization of a fluid bed system also provide for reduced real estate u~aqe due the nature of the equipment.
With the prevent invention, it it possible to utilize a higher percentage of idea fuels than way previously considered advisable in the production of white cement.
3944L/~lr-3 -12-~239~
It is intended that the foregoing be a description of a purred embodiment, but that the invention be limited solely .
by that which is within the scope of the intended claims.
With the prevent invention, it it possible to utilize a higher percentage of idea fuels than way previously considered advisable in the production of white cement.
3944L/~lr-3 -12-~239~
It is intended that the foregoing be a description of a purred embodiment, but that the invention be limited solely .
by that which is within the scope of the intended claims.
Claims (17)
1. A process of producing white cement comprising the steps of:
providing cement forming raw. materials low in coloring elements:
intermixing water. carbon bearing material and a binder with the cement forming raw materials to form a mixture:
forming the mixture into nodules:
drying the nodules:
sizing the modules to obtain a feed material having a particle size within a selected size range:
supplying the feed material to a vessel:
passing air upwardly through the material within the vessel to maintain a, fluidized bed of material within the vessel:
thermal processing the feed material within the fluidized bed by combustion of the carbon bearing material within the feed material and supplying additional fuel to the fluidized bed for maintaining the fluidized bed at a temperature in the range of approximately 2500° to 2700° F:
discharging cement clinker from the fluidized bed by displacement; and cooling the discharged clinker.
providing cement forming raw. materials low in coloring elements:
intermixing water. carbon bearing material and a binder with the cement forming raw materials to form a mixture:
forming the mixture into nodules:
drying the nodules:
sizing the modules to obtain a feed material having a particle size within a selected size range:
supplying the feed material to a vessel:
passing air upwardly through the material within the vessel to maintain a, fluidized bed of material within the vessel:
thermal processing the feed material within the fluidized bed by combustion of the carbon bearing material within the feed material and supplying additional fuel to the fluidized bed for maintaining the fluidized bed at a temperature in the range of approximately 2500° to 2700° F:
discharging cement clinker from the fluidized bed by displacement; and cooling the discharged clinker.
2. A process of producing white cement according to Claim 1 wherein the binder is white cement and is added to the raw materials at a rate of up to 5% by weight.
-13a-
-13a-
3. A process of producing white cement according to Claim 2 wherein the discharged clinker is cooled by indirect heat exchange with ambient air whereby the ambient air is heated and used for drying the nodules.
4. A process of producing white cement according to Claim 3 wherein the step of sizing the nodules includes crushing the nodules and screening the crushed nodules to obtain a feed material having a size range of approximately 14 mesh by 1/4 inch.
5. A process of producing white cement according to Claim 4 wherein the nodules are formed by extrusion.
6. A process of producing white cement according to Claim 4 wherein the nodules are formed by pelletizing the mixture.
7. A process of producing white cement according to Claim 4 further comprising the step of aging the modules after the step of drying the nodules and before the step of sizing the nodules.
8. A process of producing cement clinker comprising the steps of:
preparing a feed material by combining cement forming raw materials with carbon bearing material and cement in an amount up to 5% by weight to form a mixture and forming the mixture into nodules:
establishing and maintaining a fluidized bed of the feed material by supplying the nodules to a vessel and passing air upwardly through the material within the vessel at a velocity sufficient to maintain the nodules in a fluidized state:
thermal processing the feed material within the fluidized bed by combustion of the carbon bearing material within feed material and supplying additional fuel to the fluidized bed in an amount sufficient to maintain the fluidized bed at a temperature in the range of approximtely 2350° to 2450° F to produce cement clinker, and discharging cement clinker from the vessel.
preparing a feed material by combining cement forming raw materials with carbon bearing material and cement in an amount up to 5% by weight to form a mixture and forming the mixture into nodules:
establishing and maintaining a fluidized bed of the feed material by supplying the nodules to a vessel and passing air upwardly through the material within the vessel at a velocity sufficient to maintain the nodules in a fluidized state:
thermal processing the feed material within the fluidized bed by combustion of the carbon bearing material within feed material and supplying additional fuel to the fluidized bed in an amount sufficient to maintain the fluidized bed at a temperature in the range of approximtely 2350° to 2450° F to produce cement clinker, and discharging cement clinker from the vessel.
9. A process of producing cement clinker according to claim 8 wherein the step of preparing a feed material further includes sizing the nodules to obtain particles in the range of approximately 14 mesh by one quarter inch.
10. A process producing cement clinker according to claim 4 further comprising the step of cooling cement clinker discharged from the vessel by heat exchange with ambient air whereby the air is heated by the cement clinker and the thus heated air is utilized for drying feed material.
11. A process of producing cement clinker according to claim 10 wherein the nodules are formed by extrusion.
12. A process of producing cement clinker according to claim 10 wherein the nodules are formed by pelletizing the mixture.
13. Apparatus for producing cement clinker comprising:
a feed preparation system including means for combining cement forming raw materials with carbon bearing material, a binder and water to form a mixture and for forming the mixture into nodules, means for drying the nodules and means for sizing the nodules;
a vessel having a gas permeable grid dividing the vessel into a lower plenum chamber and an upper material chamber;
means for supplying the sized nodules to the upper material chamber:
means for supplying air under pressure to said lower plenum chamber for passage upwardly through the gas permeable grid for establishing and maintaining a fluidized bed of nodules within the upper material chamber: and means for supplying additional fuel to the upper material chamber for combustion together with the carbon bearing material within the nodules for maintaining the fluidized bed at cement clinkering temperature;
said upper material chamber having an outlet for cement clinker and an outlet for spent combustion gas.
a feed preparation system including means for combining cement forming raw materials with carbon bearing material, a binder and water to form a mixture and for forming the mixture into nodules, means for drying the nodules and means for sizing the nodules;
a vessel having a gas permeable grid dividing the vessel into a lower plenum chamber and an upper material chamber;
means for supplying the sized nodules to the upper material chamber:
means for supplying air under pressure to said lower plenum chamber for passage upwardly through the gas permeable grid for establishing and maintaining a fluidized bed of nodules within the upper material chamber: and means for supplying additional fuel to the upper material chamber for combustion together with the carbon bearing material within the nodules for maintaining the fluidized bed at cement clinkering temperature;
said upper material chamber having an outlet for cement clinker and an outlet for spent combustion gas.
14. Apparatus for producing cement clinker according to claim 13 further comprising a heat exchange flow connected to the outlet for cement clinker for cooling cement clinker discharged form the upper material chamber.
15. Apparatus for producing cement clinker according to claim 14 further comprising a heat exchanger flow connected to the outlet for spent combustion air of the vessel including means for supplying ambient air thereto for indirect heat exchange with the spent combustion air whereby the spent combustion air is cooled and the ambient air is heated and an outlet for heated ambient air flow connected to said means for supplying air to the lower plenum chamber.
16. Apparatus for producing cement clinker according to claim 15 wherein said means for forming the mixture of cement forming raw material, carbon bearing material, water and a binder into nodules is an extruder and said means for drying the nodules is a tray dryer flow connected to the indirect heat exchange for cooling cement clinker.
17. Apparatus for producing cement clinker according to claim 15 wherein said means for forming the mixture of cement forming raw material carbon bearing material, water and a binder into nodules is a pug mill and said means for drying the nodules is a tray dryer flow connected to the indirect heat exchange for cooling cement clinker.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA000498780A CA1239153A (en) | 1985-12-30 | 1985-12-30 | Method and apparatus for producing cement clinker including white cement |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA000498780A CA1239153A (en) | 1985-12-30 | 1985-12-30 | Method and apparatus for producing cement clinker including white cement |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1239153A true CA1239153A (en) | 1988-07-12 |
Family
ID=4132205
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA000498780A Expired CA1239153A (en) | 1985-12-30 | 1985-12-30 | Method and apparatus for producing cement clinker including white cement |
Country Status (1)
| Country | Link |
|---|---|
| CA (1) | CA1239153A (en) |
-
1985
- 1985-12-30 CA CA000498780A patent/CA1239153A/en not_active Expired
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