US2173182A - Cooling of cement clinker - Google Patents
Cooling of cement clinker Download PDFInfo
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- US2173182A US2173182A US251622A US25162239A US2173182A US 2173182 A US2173182 A US 2173182A US 251622 A US251622 A US 251622A US 25162239 A US25162239 A US 25162239A US 2173182 A US2173182 A US 2173182A
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- kiln
- clinker
- chambers
- cooling
- cooled
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- 238000001816 cooling Methods 0.000 title description 35
- 239000004568 cement Substances 0.000 title description 26
- 238000000034 method Methods 0.000 description 9
- 238000010276 construction Methods 0.000 description 8
- 238000007599 discharging Methods 0.000 description 7
- 230000001105 regulatory effect Effects 0.000 description 3
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000000284 resting effect Effects 0.000 description 2
- 238000007792 addition Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000010006 flight Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000033001 locomotion Effects 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000003278 mimic effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
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 specially adapted for rotary-drum furnaces
- F27B7/38—Arrangements of cooling devices
- F27B7/40—Planetary coolers
Definitions
- thez-cement madejfrom the clinker has improved rink-properties, and," in particu1ar-,f'unsoundness is eliminated or 'greatly reduced.
- Such rapidcoolingor chilling is especially important in connec- .tion with clinker-made from raw materials rel- 1 'atively high in magnesia and also aflords advan- 15 tages in the -production of cement from other
- the present invention is directed to the provision of a novel method and apparatusby which rapid cooling: or chilling of cement clinker .zuathrough thetemperature range above mentioned 1 :can be conveniently and economically effected.
- the chilling is ac- :complished by continuously adding to the hot clinker issuing from the burning zone in the 25 kiln clinker which has been cooled, the additions being made at such a rate in relation to the temperatures of the hot and cooled clinkers that the desired result is obtained.
- circulation of 30 some of the clinker: from the kiln may be advantageously employed, and in such procedure, the clinker discharging from the kiln is passed through a cooler in the usual way and a part of the cooled material is then returned to the so kiln at thedesired point.
- the cooler used for the purpose may take various forms, as, for example, it may be wholly separate from the kiln or be formedas an extension of the kiln or cons st of a plurality of cooling chambers mounted 40 longitudinally of the'kiln on the outside thereof. 7
- Means are then provided for returning a part of the cooled clinkerfto the kiln at the desired point, the construction used for this purpose depending on that of the cooler employed. 1
- FIG. 1 is a view partly in longitudinal section and partly in elevation of one form of apparatus suitable for the practice of the process of the invention
- Figs. 2, 3, and 4 are sectional views on the lines 2-2, 3-3, and, 4-4, respectively, of Fig. 1; 55 Fig. .5 is a longitudinal sectional view of an- STATES PATIENT OFFICE :Denmark; assignor to F. L. Smidth Jr 00., New York N. Y., a corporation of New Jersey Application January 18, 1939, Serial No. 251,622 I In Great Britain January 18, 1938.
- Figs. 6 and '7 are sectional views on the lines 66 and 'II, respectively, of Fig. 5.
- the apparatus shown in Fig. 1 includes a rotary kiln ill of generally standard construction having a refractory lining II with an internal dam l2, this dam being slightly beyond the end of the burning zone.
- the kiln' has the usual circumfrential tires l3 resting upon rollers l4 and 10 is rotated by any suitable means.
- the lower end of the kiln is closed by the conventional clo-' sure means l5 and thefuel for heating the kiln is supplied through a burner pipe I6 projecting into the kiln through the closure.
- the cooler takes the form of a plurality of cooling chambers ll of generally cylindrical form, the chambers being mounted longitudinally of the kiln on the outside thereof and connected to the interior of the kiln near its lower end by conduits l8.
- the cooling chambers At their lower ends, the cooling chambers have end plates l8 and are provided with spouts 20, the arrangement being such that the clinker to be discharged enters a spout and passes therefrom when the chamber from which-the spout leads is in an upper position, as illustrated in Fig. 2.
- Mounted at the ends of the cooling chambers is a hood 2
- any suitable delivery point any suitable delivery point.
- a conduit 21 leads from the end of the casing and extends around the kiln helically to a point upward from the dam l2, where the conduit is in communication with the interior of the kiln through an opening 28 through the kiln shell and lining.
- hot clinker is discharged from the kiln through the passages l8 and enters the chambers l'l through which it is advanced by gravity'as the kiln rotates. Air drawn counter-current through the chambers and into the kiln through the passages l3 cools the advancing clinker, until by the time the clinker has reached the lower ends of the chambers, its temperature has fallen within the range from about 50 C. (122 F.) to 200 0. (392 F.). A part of the clinker cooled in each or the chambers from which a conduit 21 leads enters the conduit through casing 24, and is advanced along the conduit by rotation of the kiln until it is discharged into the kiln through the opening 28.
- the amount of cooled clinker thus returned may be controlled by varying the sizes of the openings 25 from the chambers and the amount is so regulated that the returned cooled clinker is effective to chill the hot clinker issuing from the burning zone to a temperature of from 1100 C. (2012 F.) to 1200 C. (2192 F.) This chilling action occurs with such rapidity as to impart to the cement made from the clinker the desirable characteristics to which reference has been made above.
- the remainder of the cooled clinker from those chambers provided with conduits 21 and from the other chambers in the series is delivered into hopper 22 and is thence conducted through conduit 23 to the desired point.
- and the lower end of the kiln has the usual closure 32 through which extends the burner pipe 33.
- Thekiln is provided with tires 34 resting on rollers 35 and is rotated by means not shown.
- Mounted longitudinally of the kiln on the outside thereof are cooling chambers 36 connected at their lower ends to the interior of the kiln beyond the dam 3
- Within the chambers are screw flights 38 so arranged that, as the kiln rotates, the hot clinker entering the chambers through the passages is moved upward through the chambers.
- the upper ends of the chambers are open and passages 39 lead from the curved walls of certain of the chambers near the open ends to the interior of the kiln at a point just beyond the buming zone.
- a method of cooling cement clinker produced in a rotary kiln which comprises adding cooled clinker to that in the kiln at a point beyond the clinkering zone.
- a method of cooling cement clinker produced in a, rotary kiln which comprises cooling the clinker discharged from the kiln, and returning a portion of the cooled clinker to the kiln at a point adjacent the clinkering zone to be mixed with the hot clinker leaving said zone.
- a method of cooling cement clinker produced in a rotary kiln which comprises cooling the clinker discharged from the kiln, returning a portion of the cooled clinker to the kiln at a point beyond the clinkering zone to be mixed with the hot clinker leaving the zone and regulating the amount of the cooled clinker returned to insure that it will eifect rapid cooling of the hot clinker to a temperature below about 2200 F.
- a method of cooling cement clinker produced in a rotary kiln which comprises cooling the clinker discharged from the kiln by passing air over it, returning a portion of the cooled clinker to the kiln at a point beyond the clinkering zone to be mixed with the hot clinker leaving the zone, and passing the air heated by its contact with the clinker into the kiln for use in the combustion of the fuel to effect the clinkering.
- a method of cooling cement clinker produced in a rotary kiln which comprises cooling the clinker discharged from the kiln, subdividing the cooled clinker and delivering one portion to storage, and returning the other portion to the kiln at a point beyond the clinkering zone to be mixed with the hot clinker leaving the zone.
- An apparatus for producing cement which comprises a rotary kiln, means for heating the interior of the kiln, means receiving hot clinker discharging from the kiln and cooling it, and means for returning a portion. of the cooled clinker from the cooling means to the kiln at a point beyond the clinkering zone to be mixed with the hot clinker issuing from said zone.
- An apparatus for producing cement which comprises a rotary kiln, means rotatable with the kiln for receiving hot clinker discharging from the kiln and cooling it, and means for returning a part of the cooled clinker from the cooling means to the kiln at a point beyond the clinkering zone.
- An apparatus for producing cement which comprises a rotary kiln, a cooling chamber connected to the kiln and receiving hot clinker discharging therefrom, means for returning a portion of the cooled clinker from the cooling chamber to the kiln at a point beyond the clinkering zone, and means for conducting away the remainder of the cooled clinker from the chamber.
- An apparatus for producing cement which comprises a rotary kiln, a plurality of cooling chambers connected to the kiln and receiving hot clinker discharging therefrom, means for returning clinker that has been cooled in certain of the chambers to the kiln at a point beyond the clinkering zone, and means for conducting away the clinker that has been cooled in the remainder of the chambers.
- An apparatus for producing cement which comprises a rotary kiln, a plurality of cooling 75 chambers mounted on the outside of the kiln to revolve therewith, said chambers receiving clinker discharging from the kiln, means for returning to the kiln at a point beyond the clinkering zone a part of the clinker cooled'in the chambers, and means for conducting away the remainder of the cooled clinker.
- An apparatus for producing cement which comprises a rotary kiln, a cooling chamber secured to the kiln to move therewith, the interior of the chamber being connected to the interior of the kiln to receive hot clinker issuing therefrom, the clinker passing through and out of the chamber as the kiln rotates, and a passage receiving cooled clinker from the discharge endof the chamber and returning it to the kiln at a point beyond the clinkering zone.
- An apparatus for producing cement which comprises an inclined rotary kiln, a plurality of cooling chambers mounted longitudinally of the kiln on .theoutside thereof and receiving hct clinker discharging from the kiln, the clinker passing downward through the chambers as the kiln rotates and being cooled, and helical conduits mounted on the outside of the kiln and receiving *oled clinker from certain of the chambers and deli zring the clinker into the kiln beyond the clinke1 ing zone as the kiln rotates.
- An apparatus for producing cement which comprises an inclined rotary kiln, a plurality of cooling chambers mounted longitudinally of the kiln on the outside thereof, passages connecting the upper end of each chamber to the interior of the kiln, the hot clinker from the kiln entering the chambers through the passages and moving downward through the chambers to the lower end thereof as the kiln rotates, helical conduits mounted'on the outside of the kiln and leading from the lower ends of certain of the chambers to the interior of the kiln at a point beyond the burning zone, the conduits receiving cooled clinker and returning it to the kiln, and means for receiving cooled clinker from theother chambers.
- An apparatus for producing cement which comprises an inclined rotary kiln, a plurality of cooling chambers mounted longitudinally of the kiln on the outside thereof, passages connecting the upper end of each chamber to the interior of the kiln, the hot clinker from the kiln entering the chambers through the passages and moving downward through the chambers to the lower end thereof as the kiln rotates; helical conduits ker and returning it to the kiln, means for regv ulating the amount of clinker entering the conduits from the chambers from which they lead, the remainder of the cooled clinker from said chambers and from the remaining chambers being discharged, and means for receiving the cooled clinker discharged from the chambers.
- -An apparatus for producing cement which comprises an inclined rotary kiln, a chamber mounted longitudinally of the kiln on the outside thereof, a passage leading from the interior of the kiln to the lower end of the chamber, hot clinker leaving the kiln through the passage and entering the chamber, means in the chamber for moving the clinker upward through the chamber as the kiln rotates, and a passage leading from the upper end of the chamber to the interior of the kiln at a point beyond the burning zone.
- An apparatus for producing cement which comprises an inclined rotary kiln, a chamber mounted longitudinally of the kiln on the outside thereof, a passage leading from the interior of the kiln to the lower end of the chamber, hot clinker leaving the kiln through the passage and entering the chamber, means in the chamber for movingthe clinker upward through the chamber as the kiln rotates, a passage leading from the upper end of the chamberto the interior of the through the chambers as the kiln rotates and being cooled, means at the lower ends of the chambers for permitting discharge from the chambers when they are in an upper position during rotation of the kiln, means for receiving cooled clinker discharged from the chambers, and means for receiving cooled clinker from certain of the chambers and returning it to the interior of the kiln beyond the burning zone.
- An apparatus for producing cement which comprises a rotary kiln, a plurality of cooling chambers mounted longitudinally of the kiln on the outside thereof, the chambers having open upper ends, passages leading'from the kiln to the lower ends of the chambers, hot clinker entering' the chambers through the passages as the kiln rotates, means in the chambers for moving the clinker upward through the chambers as the kiln rotates, discharge passages connecting certain of the chambers near their upper ends with the kiln at a point beyond the burning zone, means for keeping the discharge passages closed throughout the major portion of the path of revolution of the chambers from which the passages lead.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
- Muffle Furnaces And Rotary Kilns (AREA)
Description
Sept. 19, 1939. E. RQNNE COOLING 0F CEMENT CLINKER U Filed Jan. 18, 1959 2 Sheets-Sheet 1 lNV TOR ATTORNEY;
Spt. 19, 1939. RQNNE COOLING OF CEMENT CLINKER Filed Jan. 18; 19:59
2 Sheets-Sheet 2 ATTORNEY;
mytmaterials. 1 3
Patented Sept. 19, v
Elna: mimic, cope This invention relates the production-of cer .ment and is concerned more'partlcularly with the cooling of cement clinker burned in a rotary kiln. u In the manufacture of cement, it is now known -51 that if the-hot clinker -ls suddenly cooled, shortly .aftcr .its formatlon;' frompthe temperature at .cvwwhich. the clinkring ,took placeto a value of Z from 1'1009J 'C.{(20 128F.)'to 1200' C. (2192 F.), thez-cement madejfrom the clinker has improved rink-properties, and," in particu1ar-,f'unsoundness is eliminated or 'greatly reduced. Such rapidcoolingor chilling is especially important in connec- .tion with clinker-made from raw materials rel- 1 'atively high in magnesia and also aflords advan- 15 tages in the -production of cement from other The present invention is directed to the provision of a novel method and apparatusby which rapid cooling: or chilling of cement clinker .zuathrough thetemperature range above mentioned 1 :can be conveniently and economically effected.
According to the'invention, the chilling is ac- :complished by continuously adding to the hot clinker issuing from the burning zone in the 25 kiln clinker which has been cooled, the additions being made at such a rate in relation to the temperatures of the hot and cooled clinkers that the desired result is obtained.
i .In the practiseof the invention, circulation of 30 some of the clinker: from the kiln may be advantageously employed, and in such procedure, the clinker discharging from the kiln is passed through a cooler in the usual way and a part of the cooled material is then returned to the so kiln at thedesired point. The cooler used for the purpose may take various forms, as, for example, it may be wholly separate from the kiln or be formedas an extension of the kiln or cons st of a plurality of cooling chambers mounted 40 longitudinally of the'kiln on the outside thereof. 7
Means are then provided for returning a part of the cooled clinkerfto the kiln at the desired point, the construction used for this purpose depending on that of the cooler employed. 1
For .a better understanding of the invention, reference may be had to the accompanying drawings in which Fig. 1 is a view partly in longitudinal section and partly in elevation of one form of apparatus suitable for the practice of the process of the invention;
Figs. 2, 3, and 4 are sectional views on the lines 2-2, 3-3, and, 4-4, respectively, of Fig. 1; 55 Fig. .5 is a longitudinal sectional view of an- STATES PATIENT OFFICE :Denmark; assignor to F. L. Smidth Jr 00., New York N. Y., a corporation of New Jersey Application January 18, 1939, Serial No. 251,622 I In Great Britain January 18, 1938.
19 Claims. (01. ass-+53) other form' of apparatus suitable for the practice of the process of the invention; and
Figs. 6 and '7 are sectional views on the lines 66 and 'II, respectively, of Fig. 5.
The apparatus shown in Fig. 1 includes a rotary kiln ill of generally standard construction having a refractory lining II with an internal dam l2, this dam being slightly beyond the end of the burning zone. The kiln'has the usual circumfrential tires l3 resting upon rollers l4 and 10 is rotated by any suitable means. The lower end of the kiln is closed by the conventional clo-' sure means l5 and thefuel for heating the kiln is supplied through a burner pipe I6 projecting into the kiln through the closure.
In the construction illustrated, the cooler takes the form of a plurality of cooling chambers ll of generally cylindrical form, the chambers being mounted longitudinally of the kiln on the outside thereof and connected to the interior of the kiln near its lower end by conduits l8. At their lower ends, the cooling chambers have end plates l8 and are provided with spouts 20, the arrangement being such that the clinker to be discharged enters a spout and passes therefrom when the chamber from which-the spout leads is in an upper position, as illustrated in Fig. 2. Mounted at the ends of the cooling chambers is a hood 2| through which the ends of the cooling chambers with'their spouts may freely move, and a hopper 22 lies within the hood in position to receive clinker discharged from the spouts 20. From the bottom of the hopper leadsa conduit 23 for conducting the discharged clinker away .to
, any suitable delivery point.
of the opening being varied by means of a plate 40 26 adjustably secured to the chamber wall. Cooled clinker passing from the chamber through the opening enters the casing and moves through the later as the chamber is carried around during rotation of the kiln. A conduit 21 leads from the end of the casing and extends around the kiln helically to a point upward from the dam l2, where the conduit is in communication with the interior of the kiln through an opening 28 through the kiln shell and lining.
With the construction described, hot clinker is discharged from the kiln through the passages l8 and enters the chambers l'l through which it is advanced by gravity'as the kiln rotates. Air drawn counter-current through the chambers and into the kiln through the passages l3 cools the advancing clinker, until by the time the clinker has reached the lower ends of the chambers, its temperature has fallen within the range from about 50 C. (122 F.) to 200 0. (392 F.). A part of the clinker cooled in each or the chambers from which a conduit 21 leads enters the conduit through casing 24, and is advanced along the conduit by rotation of the kiln until it is discharged into the kiln through the opening 28. The amount of cooled clinker thus returned may be controlled by varying the sizes of the openings 25 from the chambers and the amount is so regulated that the returned cooled clinker is effective to chill the hot clinker issuing from the burning zone to a temperature of from 1100 C. (2012 F.) to 1200 C. (2192 F.) This chilling action occurs with such rapidity as to impart to the cement made from the clinker the desirable characteristics to which reference has been made above. The remainder of the cooled clinker from those chambers provided with conduits 21 and from the other chambers in the series is delivered into hopper 22 and is thence conducted through conduit 23 to the desired point.
In the construction shown in Fig. 5, the kiln 291s provided with the usual refractory lining 30 formed with the internal dam 3| and the lower end of the kiln has the usual closure 32 through which extends the burner pipe 33. Thekiln is provided with tires 34 resting on rollers 35 and is rotated by means not shown. Mounted longitudinally of the kiln on the outside thereof are cooling chambers 36 connected at their lower ends to the interior of the kiln beyond the dam 3| by passages 31. Within the chambers are screw flights 38 so arranged that, as the kiln rotates, the hot clinker entering the chambers through the passages is moved upward through the chambers. The upper ends of the chambers are open and passages 39 lead from the curved walls of certain of the chambers near the open ends to the interior of the kiln at a point just beyond the buming zone.
Flow of air through the passages 39 and into the kiln is prevented by pivotally mounted countor-weighted plates 40, the plates being provided with cranks 4| on the outside of the passages positioned to engage a cam rail 42. The arrangement of the rail is such that the plates are moved to open position only when the ends of the passages lie below the mass of hot clinker 43 within the kiln, and throughout the remainder of the revolution of the chambers from which passages lead, the plates prevent flow of air through the passages. The clinker in the several chambers, which -.is not discharged through the passages, leaves through the open ends of the chambers and falls into a hopper 44 from which it is conducted away to a suitable delivery point.
In the operation of the apparatus shown in Figs. 5 to 7, all of the hot clinker issuing from the kiln enters the cooling chambers and is ad- 'vanced' through these chambers as the kiln rotates. In this movement, the clinker is cooled by air drawn into the kiln through the chambers. A portion of the cooled clinker leaving the chambers is then returned to the kiln to chill the hot clinker issuing from the burning zone, and the remainder of the cooled clinker is delivered to the desired storage or other point. In the constructions of both Figs. 1 and 5, the air which has been used for cooling the clinker is drawn into the kiln where it takes part in the combustion with the fuel. In the Fig. 1 construction, little or no air can enter the kiln except after having passed lengthwise through the chambers, and in the Fig. 5 construction, short circuiting oi the chambers by the air streams is prevented by the pivoted plates in the passages 39.
I claim:
1. A method of cooling cement clinker produced in a rotary kiln, which comprises adding cooled clinker to that in the kiln at a point beyond the clinkering zone.
2. A method of cooling cement clinker produced in a, rotary kiln, which comprises cooling the clinker discharged from the kiln, and returning a portion of the cooled clinker to the kiln at a point adjacent the clinkering zone to be mixed with the hot clinker leaving said zone.
3. A method of cooling cement clinker produced in a rotary kiln, which comprises cooling the clinker discharged from the kiln, returning a portion of the cooled clinker to the kiln at a point beyond the clinkering zone to be mixed with the hot clinker leaving the zone and regulating the amount of the cooled clinker returned to insure that it will eifect rapid cooling of the hot clinker to a temperature below about 2200 F.
4. A method of cooling cement clinker produced in a rotary kiln, which comprises cooling the clinker discharged from the kiln by passing air over it, returning a portion of the cooled clinker to the kiln at a point beyond the clinkering zone to be mixed with the hot clinker leaving the zone, and passing the air heated by its contact with the clinker into the kiln for use in the combustion of the fuel to effect the clinkering.
5. A method of cooling cement clinker produced in a rotary kiln, which comprises cooling the clinker discharged from the kiln, subdividing the cooled clinker and delivering one portion to storage, and returning the other portion to the kiln at a point beyond the clinkering zone to be mixed with the hot clinker leaving the zone.
6. An apparatus for producing cement which comprises a rotary kiln, means for heating the interior of the kiln, means receiving hot clinker discharging from the kiln and cooling it, and means for returning a portion. of the cooled clinker from the cooling means to the kiln at a point beyond the clinkering zone to be mixed with the hot clinker issuing from said zone.
7. An apparatus for producing cement which comprises a rotary kiln, means rotatable with the kiln for receiving hot clinker discharging from the kiln and cooling it, and means for returning a part of the cooled clinker from the cooling means to the kiln at a point beyond the clinkering zone.
8. An apparatus for producing cement which comprises a rotary kiln, a cooling chamber connected to the kiln and receiving hot clinker discharging therefrom, means for returning a portion of the cooled clinker from the cooling chamber to the kiln at a point beyond the clinkering zone, and means for conducting away the remainder of the cooled clinker from the chamber.
9. An apparatus for producing cement which comprises a rotary kiln, a plurality of cooling chambers connected to the kiln and receiving hot clinker discharging therefrom, means for returning clinker that has been cooled in certain of the chambers to the kiln at a point beyond the clinkering zone, and means for conducting away the clinker that has been cooled in the remainder of the chambers.
10. An apparatus for producing cement which comprises a rotary kiln, a plurality of cooling 75 chambers mounted on the outside of the kiln to revolve therewith, said chambers receiving clinker discharging from the kiln, means for returning to the kiln at a point beyond the clinkering zone a part of the clinker cooled'in the chambers, and means for conducting away the remainder of the cooled clinker. I
11. An apparatus for producing cement which comprises a rotary kiln, a cooling chamber secured to the kiln to move therewith, the interior of the chamber being connected to the interior of the kiln to receive hot clinker issuing therefrom, the clinker passing through and out of the chamber as the kiln rotates, and a passage receiving cooled clinker from the discharge endof the chamber and returning it to the kiln at a point beyond the clinkering zone.
clinkering zone, and means for regulating the quantity of cooled clinker entering the passage. 13. An apparatus for producing cement which comprises an inclined rotary kiln, a plurality of cooling chambers mounted longitudinally of the kiln on .theoutside thereof and receiving hct clinker discharging from the kiln, the clinker passing downward through the chambers as the kiln rotates and being cooled, and helical conduits mounted on the outside of the kiln and receiving *oled clinker from certain of the chambers and deli zring the clinker into the kiln beyond the clinke1 ing zone as the kiln rotates.
14. An apparatus for producing cement which comprises an inclined rotary kiln, a plurality of cooling chambers mounted longitudinally of the kiln on the outside thereof, passages connecting the upper end of each chamber to the interior of the kiln, the hot clinker from the kiln entering the chambers through the passages and moving downward through the chambers to the lower end thereof as the kiln rotates, helical conduits mounted'on the outside of the kiln and leading from the lower ends of certain of the chambers to the interior of the kiln at a point beyond the burning zone, the conduits receiving cooled clinker and returning it to the kiln, and means for receiving cooled clinker from theother chambers.
15. An apparatus for producing cement which comprises an inclined rotary kiln, a plurality of cooling chambers mounted longitudinally of the kiln on the outside thereof, passages connecting the upper end of each chamber to the interior of the kiln, the hot clinker from the kiln entering the chambers through the passages and moving downward through the chambers to the lower end thereof as the kiln rotates; helical conduits ker and returning it to the kiln, means for regv ulating the amount of clinker entering the conduits from the chambers from which they lead, the remainder of the cooled clinker from said chambers and from the remaining chambers being discharged, and means for receiving the cooled clinker discharged from the chambers.
16. -An apparatus for producing cement which comprises an inclined rotary kiln, a chamber mounted longitudinally of the kiln on the outside thereof, a passage leading from the interior of the kiln to the lower end of the chamber, hot clinker leaving the kiln through the passage and entering the chamber, means in the chamber for moving the clinker upward through the chamber as the kiln rotates, and a passage leading from the upper end of the chamber to the interior of the kiln at a point beyond the burning zone.
17. An apparatus for producing cement which comprises an inclined rotary kiln, a chamber mounted longitudinally of the kiln on the outside thereof, a passage leading from the interior of the kiln to the lower end of the chamber, hot clinker leaving the kiln through the passage and entering the chamber, means in the chamber for movingthe clinker upward through the chamber as the kiln rotates, a passage leading from the upper end of the chamberto the interior of the through the chambers as the kiln rotates and being cooled, means at the lower ends of the chambers for permitting discharge from the chambers when they are in an upper position during rotation of the kiln, means for receiving cooled clinker discharged from the chambers, and means for receiving cooled clinker from certain of the chambers and returning it to the interior of the kiln beyond the burning zone.
19. An apparatus for producing cement which comprises a rotary kiln, a plurality of cooling chambers mounted longitudinally of the kiln on the outside thereof, the chambers having open upper ends, passages leading'from the kiln to the lower ends of the chambers, hot clinker entering' the chambers through the passages as the kiln rotates, means in the chambers for moving the clinker upward through the chambers as the kiln rotates, discharge passages connecting certain of the chambers near their upper ends with the kiln at a point beyond the burning zone, means for keeping the discharge passages closed throughout the major portion of the path of revolution of the chambers from which the passages lead.
and means for receiving cooled clinker discharged 5 from the open ends of the chambers.
EINAR mam.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB2173182X | 1938-01-18 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2173182A true US2173182A (en) | 1939-09-19 |
Family
ID=10900381
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US251622A Expired - Lifetime US2173182A (en) | 1938-01-18 | 1939-01-18 | Cooling of cement clinker |
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| Country | Link |
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| US (1) | US2173182A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2483738A (en) * | 1944-11-09 | 1949-10-04 | Smidth & Co As F L | Cooler |
| US2507123A (en) * | 1947-01-31 | 1950-05-09 | Int Nickel Co | Rotary kiln for chemical and metallurgical processes |
| US2549787A (en) * | 1947-11-21 | 1951-04-24 | John B Dube | Calcining kiln |
| US2904322A (en) * | 1955-03-15 | 1959-09-15 | Elektrokemisk As | Arrangement for discharge of material from rotary kilns |
| US2921779A (en) * | 1957-10-14 | 1960-01-19 | Monolith Portland Midwest Comp | Rotary kilns |
-
1939
- 1939-01-18 US US251622A patent/US2173182A/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2483738A (en) * | 1944-11-09 | 1949-10-04 | Smidth & Co As F L | Cooler |
| US2507123A (en) * | 1947-01-31 | 1950-05-09 | Int Nickel Co | Rotary kiln for chemical and metallurgical processes |
| US2549787A (en) * | 1947-11-21 | 1951-04-24 | John B Dube | Calcining kiln |
| US2904322A (en) * | 1955-03-15 | 1959-09-15 | Elektrokemisk As | Arrangement for discharge of material from rotary kilns |
| US2921779A (en) * | 1957-10-14 | 1960-01-19 | Monolith Portland Midwest Comp | Rotary kilns |
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