This invention is for improvements in or relating to the manufacture of cementitious materials and ⁴ is particular¬ ly concerned with providing an improved method and apparatus for use in the manufacture of cementitious materials. 5. In the manufacture of cementitious materials it is known to provide a rotating kiln in which raw feed material is fed in at one end. The kiln is rotated and is inclined at an angle to the horizontal such that the raw feed is fed in at the upper end of the kiln and as the kiln rotates 0 the raw feed has water evaporated therefrom (if the raw feed is wet) as a result of heat being applied to the lower end of the kiln. The raw feed gradually dries to a non-liquid state, carbon dioxide is driven off from what is then rela¬ tively solid material and then that material is rendered 5- into a clinker in a zone of the furnace known as the burning zone, before being cooled.

Heat which is supplied to a kiln may either be by a burner using a fossil fuel such as for example, coal, oil or gas or the kiln may have heat supplied thereto by 0 electricity.

-> The ^' present invention is applicable to any form of a rotating kiln for use .in the manufacture of a cementitious material.

It will be appreciated that in order to form the 5 cementitious material the raw feed has not only to have the moisture evaporated therefrom, but has to be heated to a

sufficiently high temperature in order to calcine the material into a cementitious clinker. This cementitious clinker after cooling is subsequently ground to a powder in a mill and mixed with other materials in order to form a cementitious product. The clinker is formed in the burning zone and it is necessary thereafter to cool that clinker for storage and subsequent transportation. It will be appreciated that the clinker possesses heat and if the clinker is allowed to leave the kiln with that heat, some of that heat will be wasted.

An object of the present invention is to remove some of the heat from the clinker, as it is cooling and transfer it to the cooler air entering the kiln.

It will also be appreciated that at the ⁴ entry of the raw feed to the kiln hot gases are leaving the kiln to pass up a_ chimney and it is an object of the present inven¬ tion to transfer some of the heat from such hot gases to the raw feed as it enters the kiln.

Accordingly, the present invention provides a method ^' of manufacturing a cementitious material in a rotating cement making kiln having gases passing therethrough which comprises rotating the kiln, . providing at least one ring of lifting members for the material around the internal periphery of the kiln to lift the material from the bottom of the kiln and allowing the material tc fall out of the lifting members to the bottom of the kiln.

In order to assist the transfer of heat between the gases within the kiln and the material which commences as the raw feed and exits the kiln as a cementitious clinker the invention provides for the lifting of the material from the bottom of the kiln along which it progresses. It will be appreciated that the material lies mainly on the bottom of the kiln and _^ is lifted partly to one side as the kiln rotates. After a few degrees of rotation from the bottom the material falls back again to the bottom.

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It i.s desired therefore to lift the material further up the side of the kiln and over the top dead centre of the kiln in order to expose a greater surface of said material to the gases and thus to effect a better exchange of heat between the two. . Such exchange of heat is froir. gases to raw feed at one end of the kiln and from hot clinker to cooler air at the other or lower end of the kiln, i.e. where the clinker leaves the kiln. The term kiln as used herein includes not only a kiln in which the cementitious clinker is made but inclu¬ des for the purposes of this specification a rotating member into which hot cementitious clinker may be fed for cooling thereof, such member will be rotatable about a substantially horizontal axis and cool air will enter such member and after exchange with the heated clinker the air " passes into- the kiln in which the raw feed is calcined to cementitious clinker.

Accordingly the present invention provides a rotating kiln for the manufacture of cementitious material said kiln comprising an elongate tubular member mounted for rotation about an axis inclined to the horizontal, means for feeding material into the kiln and means for permit¬ ting the exit of material from adjacent to the lower end of the kiln characterised in the provision of at least one ring of lifting members on the interior periphery of the kiln, said members having the means to lift the mater¬ ial from adjacent the bottom of the kiln and allow the material to drop back to the bottom of the kiln.

The lifting members have an inlet opening through which the material enters and an exit opening from which the material leaves and a passageway between the two open¬ ings so that as the kiln rotates, material held in the passageway between the two openings will subsequently fall from the said exit opening down to the bottom of the kiln again. The lifting members may comprise a series of tubes

secured to the internal periphery of the kiln or they may be formed of refractory material by building blocks of desired material or of refractory material cast in situ within the kiln. The exit opening will desirably be of larger size than the inlet opening

The lifting members will be in the form of a ring on the internal periphery of the kiln and a plurality of rings may be provided, each ring being separated by a banker ring or other means which restricts the flow of the material from one ring to the next, thus ensuring that the material is retained longer within the lifting members and thus lifted higher. The lifting members may if desired have a passageway extending radially inwardly so that the material may fall out of the lifting members apart from out of the exit opening of the members. The passageway through the lifting members from one opening to the other may either be parallel to the axis of rotation of the kiln or may be inclined thereto. Said angle of inclination may either be in the direction of rotation of the kiln in which event it will as'sist the material to pass more rapidly through the lifting member, or may be in the oppos¬ ite direction to that of rotation of the kiln in which case it will reduce the speed at which the material passes . through the lifting member. By effecting a transfer of heat between the raw feed or cementitious clinker on the one hand and the gases in the kiln, it is thought that for the same amount of heat fed to the kiln-a greater amount of cementitious clinker will be produced or alternatively less heat will be needed by the kiln to produce the same quantity of cementitious clinker.

Reference is made to the drawings, in which: Figure 1 is an elevation of a wet-feed cement kiln; Figure 2 is a diagrammatic representation of a dry- feed cement kiln;

Figure 3 is a diagrammatic representation of a cement kiln having a cooler;

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Figure 4 is s longitudinal cross-section of a, portion of a cement kiln having one form of lifting members; Figure 5 is a section on the line x-x in Figure 4, divided into four parts showing alternative constructions; Figure 6 is a longitudinal cross-section of a portion of a cement kiln having an alternative form of lifting members; Figure 7 is a section on line y-y in Figure 6; and Figures 8 to 16 are cross-sections corresponding to Figures 10, 11, 13, 14 and 15 being divided into three parts and Figure 16 into two . parts, each part in any one Figure showing ^" alternative configurations for lifting members of the same general shape. .. Referring first to Figure 1, a cement kiln comprises an elongate tubular steel body 1 supported on roller 2 at a small inclination to the horizontal. The body 1 is rotated by means of an electric motor 3 turning a pinion 4 in engagement with a ring gear 5. The body 1 is lined with refractory bricks, which are not shown in detail. A burner pipe 6 extends into the body 1 from the lower end thereof and is supplied with air from a blower 7 and pulverised coal through a coal feed pipe 8.

The pulverised coal blown into "the body 1 burns as a jet which strikes the brick lining of the body 1 (or rather, in use, the materials forming the cement clinker on the lining) raising the temperature to a level sufficient for the cement clinker forming reaction to occur.

The cement-forming materials are introduced in the form of an aqueous slurry into ^' the body 1 of the kiln at the upper end thereof, as indicated by arrow S. The materials pass down the kiln through a conventional chain section 9, in which the slurry is dried and broken into a powder, and which forms.part of pre-heating zone A, to a

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C0 ₂ zone B, in which carbon dioxide is driven ^' off, and thence to a burning zone C, in which the temperature is sufficient to enable the. ^' cement clinker forming reaction to take place. ^' The powdered materials fuse during the reaction

^" 5 and on moving down past the burning ^' zone C into a cooling zone D form a cement clinker. The clinker leaves the body 1 through apertures 10, passing through heat exchanges 11 in which heat may be transferred to the combustion air entering the kiln, improving combustion efficiency.

10 Rings 12 of the lifting members which may,.for example, have the form illustrated in any of Figures 4 to 16, as hereinafter described, are mounted within the kiln body 1 at a location just upstream of the apertures 10, just upstream of the burning zone C and at the upper end of

15. the .body 1. The lowermost rings 12d serve to transfer heat from the hot clinker to the combustion air passing up the body 1 towards the flame. The middle rings 12b transfer heat to the material from the hot gases from the burning zone, raising the temperature of the material

20 more rapidly to that at which the carbon dioxide is driven off. The uppermost rings 12a transfer heat at a lower temperature from the gases leaving the kiln body in the direction of arrow G to the slurry entering the kiln body 1. The dry-feed kiln illustrated in Figure 2 does not

25 require the long pre-heating drying zone used in wet-feed •kilns. The combined pre-heating and CO- zone B has a series of rings 12b of lifting members in which the material is raised towards the burning temperature, and rings 12d adjacent to the clinker outlet of the kiln to

30 cool the clinker and pre-heat the combustion air.

The kiln body 1 of Figure 3 may be of either the wet- feed or dry-feed type. The pre-cooled clinker leaving the lowermost rings 12d of lifting members passes into an external cooler 30 in which a series of rings 31 of lifting

35 members is arranged. The cooler 30 rotates in a similar

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manner to the kiln, and.air is passed through the cooler in the direction of arrow 1 , some of the air being drawn t rough the ^" blower supplying air to the burner pipe 6 Very efficient heat transfer from the clinker to the air is obtained; the clinker leaving the cooler 30 can be sufficiently cool to handle manually.

Whilst the kilns described with reference to Figures 1, 2 and 3 are shown with coal or gas fired burner ^' s the invention is equally applicable to kilns having other forms of heating, for example electricity.

Figures 4 and 5 illustrate forms of lifting members which may be constructed in refractory brick or ceramic materials and thus be suitable for use in or near the high temperature burning zone C of the kiln. Figure ^* 5 is a view up the kiln toward the inlet for the materials. The steel, shell 40 of the kiln has a lining of refractory bricks 41 except where the rings of lifting members are provided. The lifting members are formed as refractory blocks 42 mounted around the inner surface of the shell 40. The blocks 42 have an inlet opening 43a_ through which the material passes t enter a passageway 43 leading to an exit opening 43b through which the material leaves the block 42. The surface of the passageways 43 are generally parallel to the surface of the shell 40 at their nearest points to the shell 40, but slope inwardly towards the axis of the kiln at their nearest points to the axis. Thus " the inlet openings 43a are smaller than the exit openings 43b. Adjacent rings of blocks 42 are separated from each other by banker rings 44 formed of refractory bricks which are tapered on the surface facing inwardly of the kiln. These banker rings- serve to reduce further the size of the inlet openings 43a thereby holding back the material in its pas¬ sage down the kiln and allowing time for the rotation of the kiln to lift the material up the side of the kiln. The sectors 5A, 5B, 5C and 5D show alternative arrangements of refractory block 42 which can make up the rings of lifting members. Sector 5D shows the passageway 43 having a

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tapered tubular lining member 45 which may serye to reduce abrasion of the Blocks by material passing through the passageway 43. ^' The lining member ^' s 45 will be formed of a refractory- material, which may be ^" a ceramic or a i metal, where the rings are located at a high temperature zone of the kiln.

In use, the material will flow down the kiln in the direction of arrow M in Figure 4. The lifting members serve several main functions. Firstly, the material tends to bank up on the upstream side of each ring and this causes the material to ride higher up the side of the kiln as the kiln rotates, thus presenting a larger surface area to the gases flowing up the kiln. Secondly, some of the material is carried around the kiln, as it rotates, by the passageways 43. Thirdly, some of the - material carried by the passageways 43 tend to fall out as the blocks pass over the top of their rotation path, the inward taper of the passageway 43 assisting this falling out, the resultant fall of material, which may form a 'curtain' across the kiln, greatly increasing the surface area of material in contact with the gases. Fourthly, as the material passes through the passageway 43 in the blocks, heat is transferred between the blocks and the material, and as the blocks travel around the remainder of their circular path they are again heated or cooled by the gases flowing in the kiln. The direction ^* of heat transfer will depend upon the location of the rings; upstream of the burning zone heat is transferred from the gases to the material via the blocks, and down- stream heat is transferred from the material to the air. The banker rings 44 delay passage of the material down the kiln through the rings and thus serve to increase contact time of the material with the rings and thus heat transfer. In some constructions the banker rings may be omitted.

The lifting members shown in Figures 6 and 7 are

intended primarily for. use at .the. uppermost end of a wet- feed kiln, the member comprising tapered tubular steel bodies 60 mounted on the lining bricks 61 of the shell 40 of the kiln by means of brackets 62 passing through or between the bricks ^' 61 and welded to the inner surface of the shell 40. The bodies 60 are partially closed at each end by steel grilles 63, and contain steel balls 64, or similar pieces of metal, which serve to scour the insides of the bodies 60, preventing blockage by the slurry passing through in addition to further improving heat transfer Banker rings 44, as described with reference to Figures 4 and 5, separate the rings of bodies 60.

Figures 8 to 11 show alternative shapes of passageways through the rings of lifting ^' members, similar to those shown in Figures 4 and 5. In figures 8 and 9, tapered passageways are shown as before, whilst in Figures 10 and

11, untapered passageways are shown. Sectors 10A and

11A show passageways whose axes are parallel to that of the kiln, whilst Sectors 10B and 11B show passageways whose axes are inclined to the direction of rotation of the _, kiln so as to slow the passage of material through the lifting members. The inclination referred to is clearly illustrated in the Figures. The passageways shown in Sectors 10C and 11C are inclined in the opposite direction of the passageways of Sectors 10B and 11B so as to accelerate the flow of material through the lifting member. These alternative configurations enable control to be exercised locally of the flow rate and hence heat transfer. Combin¬ ations of such different rings may be used. Figures 12 to 16 show various forms of an alternative arrangement of lifting members having passageways 120 through the blocks 121 forming the ring, the passageways 120 also opening radially inwardly of -the kiln. This arrangement ensures that a greater proportion or all of the material carried up in the passageways falls out as the passageways pass over the top of their path.. Figure 12 shows passageways having an inner surface 122 which is inwardly tapered in the

same manner as the inner surface, of .the passageways in, for example, the embodiment of Figure ^' 8, to assist the material in falling out. Figure 13 shows ^' three sets of passageways similar to that of Figure 12, but without the inward taper. In Sector A of Figure 13 the passageways pass straight through the ring, whilst in Sectors B and C the passageways are inclined relative to the direction of rotation of the kiln so as to slow passage of the material, in the case of 13B, or accelerate, in the case of 13C. • Figures 14 and 15 are generally similar to Figure 13, showing alternative shapes of passageways, whilst Figure 16 shows passageways which are twisted, -rather than simply inclined to the kiln axis, the type shown in Sector B tending to slow the material, whilst that in Sector C tends accelerate its passage down the kiln.

All rings ^' of Figures 8 to 16 are shown from a position looking up the kiln towards the end at which the materials are introduced into the kiln. The rings may be formed from blocks of any suitable shape, as shown in Figure 5. A kiln having lifting members as. described will, by virtue of the more efficient heat transfer to and from the material passing through it, the sintering process depend¬ ing less on radiant heat from the lining, wasteless heat by radiation from the kiln and in 'the gases and clinker leaving the kiln. Thus the throughput may be increased for a given energy consumption, or the energy consumption may be reduced for a given throughput of material.

A new kiln in accordance- with the invention may be built shorter than conventional kilns of the same capacity, with consequent savings in capital expenditure.