Hope

Location:

Clinker manufacture operational: 1929 to date

Approximate total clinker production to 2022: 76 million tonnes (1st)

Raw materials:

Ownership:

After 29 years of Blue Circle’s existence, Hope was its first UK green-field site. The next was Cauldon, 28 years later. The plant seems to have been planned as early as 1910, but plans were disrupted by WWI and the ensuing volatile economy. The site has raw materials perfect for dry process, but, installed at a time when the reputation of dry process was at its lowest ebb, wet processing was adopted. Uniquely among plants at the time, Hope was prohibited from discarding kiln dust from the outset, and recycled all its wet process dust in A1 and A2 slurry feeds. The plant became Blue Circle’s largest following installation of A5 in 1953 until 1962 when it was overtaken by Cauldon. The planning of the kiln A5 expansion caused a furore during 1949-1952, not because of the capacity expansion, but because of the accompanying new 120 m stack, although the existing plant, with no dust fitration, was already very prominent in the National Park landscape. Electrostatic precipitators were fitted to the existing kilns as part of the project, and dust emissions were dramatically reduced. The existing site became very cramped with the expansion, and when further expansion was called for, it was obvious that a new kiln area should be used. By that time, sufficient confidence had been gained in the Plymstock kilns to install two large KHD suspension preheater kilns. This became part of the major rationalization of Blue Circle’s capacity that also involved the construction of Northfleet, and accordingly the plant was nearly doubled in size. Kilns B1 and B2 ran neck-and-neck with the Northfleet kilns as the largest until they were overtaken by Platin A2 in 1977.

The plant had from the outset a purpose-built 3 km spur from the main Manchester-Sheffield railway, and this allowed easy transport into Earle’s depot network throughout the North. More recently, because the nearby Cauldon lacks rail, Lafarge considerably up-rated Hope’s rail facilities so that it could serve the longer-distance market with Cauldon covering the immediate area.

Please contact me with any relevant information or corrections. I am particularly interested in firmer dates and statistics.

Note: technical information on currently operational plants is ✄withheld in the public version of the site at present, except where already published (see references).

Power Supply

The plant was electrically powered from the outset, using power purchased from the Yorkshire Electric Power Co., subsequently from the grid.

Rawmills

Seven rotary kilns were installed in five stages:

Kiln A1

Supplier: FLS
Operated: 15/11/1929 to 25/05/1970
Process: Wet
Location: Hot end 416733,382198: Cold end 416665,382152: entirely enclosed
Dimensions (from cooler ports): Metric:

Rotation (viewed from firing end): anti-clockwise
Slope: 1/25 (2.292°)
Speed: ?
Drive: ?
Kiln profile (from cooler ports):

Cooler: Unax planetary 12 × 4.85 × 1.060
Fuel: Coal
Coal mill: semi-indirect: ?Earles ball mill, later operated direct
Exhaust: via ID fan direct to stack: an electrostatic precipitator was put in after the ID fan in 1953.
Typical Output: 1929-1941 266 t/d: 1941-1946 260 t/d: 1946-1958 275 t/d: 1959-1970 258 t/d
Typical Heat Consumption: 1929-1937 6.43 MJ/kg: 1937-1942 7.04 MJ/kg: 1943-1954 7.39 MJ/kg: 1955-1970 7.85 MJ/kg


Kiln A2

Operated: 25/11/1929 to 25/05/1970
Location: Hot end 416738,382191: Cold end 416671,382144: entirely enclosed
Dimensions (from cooler ports): Metric:

Kiln profile (from cooler ports):

Typical Output: 1929-1941 264 t/d: 1941-1946 260 t/d: 1946-1958 278 t/d: 1959-1970 255 t/d
Typical Heat Consumption: 1929-1937 6.57 MJ/kg: 1937-1942 7.21 MJ/kg: 1943-1954 7.49 MJ/kg: 1955-1970 7.86 MJ/kg
Identical in all other respects to A1

Kiln A3

Supplier: Vickers Armstrong
Operated: 23/04/1935 to 31/05/1970
Process: Wet
Location: Hot end 416747,382186: Cold end 416675,382137: entirely enclosed
Dimensions (from cooler ports):

Rotation (viewed from firing end): ?
Slope: ?
Speed: ?
Drive: ?
Kiln profile (from cooler ports):

Cooler: Reflex “Recuperator” planetary 12 × 13’6⅜”×4’0” (metric 4.12 × 1.207)
Fuel: Coal
Coal mill: semi-indirect: ?Earles ball mill, later operated direct
Exhaust: via ID fan direct to stack: an electrostatic precipitator was put in after the ID fan in 1953.
Typical Output: 1935-1951 315 t/d: 1952-1970 326 t/d
Typical Heat Consumption: 1935-1961 7.27 MJ/kg: 1962-1970 7.63 MJ/kg


Kiln A4

Supplier: Vickers Armstrong
Operated: 1938 to 31/05/1970
Process: Wet
Location: Hot end 416752,382179: Cold end 416681,382130: entirely enclosed
Dimensions (from cooler ports):

Rotation (viewed from firing end): ?
Slope: ?
Speed: ?
Drive: ?
Kiln profile (from cooler ports):

Cooler: Reflex “Recuperator” planetary 12 × 14’6⅜”×4’0” (metric 4.43 × 1.207)
Fuel: Coal
Coal mill: semi-indirect: Rema closed circuit ball mill, later operated direct
Exhaust: via ID fan direct to stack: an electrostatic precipitator was put in after the ID fan in 1953.
Typical Output: 1938-1944 341 t/d: 1944-1950 334 t/d: 1950-1957 339 t/d: 1958-1963 333 t/d: 1964-1970 339 t/d
Typical Heat Consumption: 1938-1962 7.40 MJ/kg: 1962-1970 7.79 MJ/kg


Kiln A5

Supplier: Vickers Armstrong
Operated: 4/1953 to 30/05/1970
Process: Wet
Location: Hot end 416731,382209: Cold end 416646,382150: a short part of the hot end was enclosed
Dimensions (from cooler ports): 338’10½”× 11’6”B / 10’0¼”CD (metric 103.29×3.505B/3.054CD)
Rotation (viewed from firing end): ?
Slope: 1/24 (2.388°)
Speed: ?
Drive: ?
Kiln profile (from cooler ports): -610×3353: 1422×3353: 4089×3505: 29794×3505: 32461×3054: 101765×3054: 102375×2121: 103289×2121: tyres at 6960, 22860, 39929, 59436, 78943, 98450: turning gear at 42748
Cooler: Reflex “Recuperator” planetary 12 × 14’6⅛”×4’0” (metric 4.42 × 1.207)
Fuel: Coal
Coal mill: direct: two No.18 Atritors
Exhaust: ID fan followed by electrostatic precipitator.
Typical Output: 1953-1961 426 t/d: 1962-1970 430 t/d
Typical Heat Consumption: 1953-1961 7.33 MJ/kg: 1962-1970 7.62 MJ/kg


Kiln B1

Supplier: kiln by Polysius: preheater by KHD
Operated: 01/04/1970 to date
Process: suspension preheater: details✄
Location: hot end 416587,382400: cold end 416532,382443: unenclosed
Dimensions: Metric 70.00 × 4.770(1)
Rotation (viewed from firing end): anticlockwise
Slope: ?
Speed: 0.284-1.7 rpm(1)
Drive: 330 kW(1)
Kiln profile: ✄
Cooler: grate: details✄
Fuel: coal, plus tyres from 1981, petcoke from 1985, meat and bone meal from 2004 and sewage sludge from 2011.
Coal mill: direct: ✄
Exhaust: ✄
Typical Output: ✄
Typical Heat Consumption: ✄


Kiln B2

Operated: 22/05/1970 to date
Location: hot end 416596,382411: cold end 416541,382454: unenclosed
Rotation (viewed from firing end): clockwise
Typical Output: ✄
Typical Heat Consumption: ✄
Identical in all other respects to B1


References:

Sources:

The following is based on anonymous articles describing the plant as originally constructed. One appeared in Cement and Cement Manufacture, III, 1930, pp 55-68. Another was a pubicity pamphlet published by BPCM in 1929, including much the same text and pictures. Both are believed to be out of copyright. Both are provided, since they have somewhat different emphasis - the pamphlet was designed for a less technical audience, but contains more information.

Values of imperial units (as of 1929) used in the text: 1 inch = 25.399956 mm: 1 ft = 0.30479947 m: 1 cubic ft = 0.0283167 m3: 1 ton = 1.01604684 tonne: 1 HP (horse-power) = 0.7456998 kW: 1 psi (pound-force per square inch) = 6.89478 kPa.

First, the article in Cement and Cement Manufacture:

The New Hope Cement Works of Messrs. G. & T. Earle, Ltd.

Hope 1 Figure 1. View of the plant from the quarry.

Hope 2 Figure 2. Sketch plan of the plant.

Hope 12 Figure 12. Ruston & Hornsby electric shovel loading blasted limestone. The drill-rig is in the background.

Manufacture of Portland cement was recently commenced at the new factory of Messrs. G. & T. Earle. Ltd., cement manufacturers, of Hull (Note 1). The site selected is at Hope, on the south-eastern border of the High Peak district of Derbyshire, about midway between Manchester and Sheffield. A private railway connects with the Dore and Chinley branch of the London, Midland and Scottish Railway Company, while road transport for the finished product will be facilitated by the construction of a concrete road from the works to the main road leading from Hathersage to Castleton. A brief summary of the directions in which accepted practice has been departed from, and new ideas so far as Great Britain is concerned are now being tried out, will be of interest.

For the first time a gyratory crusher for fine crushing in cement works is being used (Note 2). Exit gases are led directly into dust-collecting fans. Only three elevators have been fitted throughout the works; one of them lifts coal from the railway wagons into the storage hoppers, the second is for fine coal storage, and the third restores dust from the kiln induced-draught fans back into the kilns. The processes of crushing, grinding, kiln slurry feeding, and the preparation of the clay are all accomplished without the aid of a bucket elevator. There is no tramway in connection with clay-winning and washing. The clay is dragged by scraper gear direct from the clay-field into a clay washmill and thence pumped into storage.

The factory is laid out for a cement production of 3,200 tons per week and arranged with a view to future extensions (Note 3). On visiting the site attention is immediately arrested by the hilly nature of the ground, and one appreciates that the lay-out of the quarries and plant has been to a large extent determined by the contours of the ground. The quarry floor is 875 ft. above ordnance datum, the works themselves finish with the clay washmill at 570 ft. O.D.; thus there is a difference of 305 ft. from highest to lowest levels.

The Quarry

The limestone is of high quality, practically free from moisture, and contains 97 per cent. of calcium carbonate. A quarry face about 700 ft. in length was opened during the construction of the factory in preparation for large-scale blasting. Shortly before manufacture commenced, the drilling of this face was completed, and at one operation about 30,000 tons of limestone were dislodged and broken to a suitable size for picking up by the electric navvy. The holes, drilled by well drills of the company's own manufacture, were 6 in. in diameter by 35 ft. deep and were exploded simultaneously.

The broken limestone is picked up by an electric navvy with a bucket of 3½ cu. yd. capacity and caterpillar wheels for travelling. The slewing of the jib is accomplished by a self-contained unit operated by its own motor; in fact, a separate motor is provided for each motion. A 110-HP motor takes care of the hoisting, while slewing and racking each has its own 40-HP power units. Each of the three motions is controlled by a separate reversing-contactor type stator panel with mechanical and electrical interlocks and over-load relays. Master controllers fitted with vertical hand-levers actuate these contactors, while two-pole overload protection is provided throughout. Clutches are operated pneumatically with a minimum of effort from the chargeman. The controls provided fully protect the motors, which can be stalled for a considerable interval without damage.

The two electric locomotives used to convey the limestone from the quarry face to the crusher house are each driven by two 27-HP motors and are capable of taking a 50-ton load up the steepest quarry gradient, which is 1 in 50, at a speed of 10 miles per hour. Direct current is collected by two collector shoes in contact with a third rail in the centre of the track. The 400-volts 3-phase current is converted to a 250-volt D.C. supply with earthed return to provide the necessary power for these locomotives. Steel wagons of standard gauge and of 7-cu. yd. capacity are used for conveying limestone to the crusher house.

Hope 5 Hope 6 Figures 5 & 6. Primary jaw crusher - Ross feeder right, with a 9-ton wagon of stone about to be tipped. It was later replaced with a gyratory crusher.

In the crusher house building is installed the largest jaw crusher yet built in England, having a 6 ft. by 4 ft. opening and weighing about 133 tons. It is capable of taking blocks of stone weighing five tons and crushing them down to 6 in. size, the output being about 250 tons per hour. This crusher is driven by a 250-HP motor, and the crushed stone proceeds to a secondary crusher of the gyratory cone type.

Hope 7 Figure 7. Symons secondary cone crusher.

The latter crusher differs from the usual run of gyratory crushers in that it has a very much higher speed (about 450 r.p.m.) and the cone is flattened towards the base. In the standard gyratory crusher the largest size stone which can fall through is determined by the distance between the cone and casing at its widest. In this fine crusher, however, the flattened cone and the high speed delay the exit of the crushed material for at least one complete revolution of the mill. It therefore follows that the largest size stone is regulated by the distance between the closed side of the cone and the casing, and not by the open side. The shock of the crushing is taken by about forty spiral springs, the tightness of which, and the size of the crushed product, can be regulated while the machine is running. The weight of this crusher is about 50 tons and its output 225 tons per hour when crushing down to ½ in. size from 12 in. blocks. It is the largest crusher of its type in England.

There is a drop of 198 ft. down the hillside between the jaw crusher entrance and the top of the limestone silos, and this has to be provided for. From the quarry floor to the jaw crusher the stone falls 28 ft. and from thence to the secondary cone crusher intake a belt conveyor 353 ft. long by 42 in. wide lowers the stone a distance of 59 ft. to the cone crusher. The final descent down the hillside is by a chute in which heavy chains are arranged to check the flow of the stone before reaching a belt conveyor which conveys it to the limestone silo. This silo is built in reinforced concrete and has a capacity of 2,000 tons of stone, and from here the crushed limestone is led direct to the feed tables of two combination mills each 36 ft. long by 7 ft. 2½ in. diameter and driven by 650-HP auto-synchronous motors through reduction gearing.

The raw mills, as well as the dry mills mentioned later, are driven direct from the reduction gearing through a coupling and shaft fixed to the mill in line with the axis, thus dispensing with the pinion and spur-ring wheel usually provided for tube mills (Note 4).

The slurry from the raw mills is run through a motor-driven mechanically-vibrated screen which takes out any coarse matter before the slurry passes to the centrifugal pumps which convey it to the storage tanks. The slurry storage is accommodated in five reinforced concrete tanks each of about 17,000 cu. ft. capacity (Note 5), which have no mechanical stirring gear but are provided with compressed-air mixing arrangements through fixed pipes at the bottom of each tank.

Clay Plant

Hope 11 Figure 11. Dragline in clay field.

In the clayfield a washmill of 20 ft. diameter, provided with a 104-HP motor, washes the clay at the rate of 60 tons per hour, from which point it is pumped to the works by plunger pumps into two clay tanks each holding about 620 tons of clay. The method of winning the clay is by means of a scraper digger having a 3-yd. bucket and capable of an output of 60 tons per hour with a maximum length of haul on the ropeway of 830 ft. A 150-HP motor provides power for this scraper, which, working one shift per day, provides clay sufficient for the output of the factory.

From the clay washmill the "slip" is pumped to the works 780 yds. distant, where it is stored in two clay tanks each holding 620 tons of clay "slip". From these tanks the "slip" gravitates through a float-valve into a measuring tank from whence two bucket wheels with variable-speed control supply measured quantities to the mills, also by gravity (Note 6). The means by which the "slip" in the measuring tank is kept at constant level by means of a float valve is of interest. The float, instead of acting directly upon the valve, is fitted with contactor gear and a small motor which turns the valve wheel backwards and forwards according to the varying pressures from the clay tank and the filling requirements of the mills.

Kiln House

Hope 3 Figure 3. Kilns - view towards front end.

Hope 4 Figure 4. Kilns and coolers from the firing floor.

Hope 8 Figure 8. 650 HP motors and Symetro gear boxes for the two rawmills.

Two kilns are housed in the kiln building, which also accommodates the coal grinding mills. The kilns are 276 ft. long by 8 ft. 4½ in. diameter with enlarged burning zones 46 ft. long by 10 ft. 4 in. diameter (Note 7), each having a rated capacity of about 10 tons of clinker per hour. The coolers are of the latest design, comprising twelve integral coolers arranged around the periphery of the kiln itself. These coolers are fitted with a large number of hanging chains which, as the kiln rotates, alternately become buried in the clinker and acquire part of the clinker heat in order to give it out again to the ingoing cold air when the movement of the kiln raises them from the hot clinker.

From the kilns the clinker drops on to a belt conveyor made of special fabric and designed to withstand hot temperatures. This conveyor carries the clinker into a small pit which is emptied at frequent intervals by means of an overhead crane and grab which dumps the clinker into a store having a capacity of 3,350 tons at floor level (Note 8).

In the kiln house building behind the burner's platform is situated the coal-grinding plant. This consists of combination ball and tube mills through which hot air from the clinker coolers passes, thus combining the operation of drying and grinding and dispensing with the necessity for a coal drier (Note 9). The coal is recovered from the hot air by means of a cyclone and elevated to fine coal storage bins, thus enabling the coal mills to be shut down at intervals for repairs and also enabling them to be run at full output when the kiln consumption is less than the mill capacity.

Coal is received at the works sidings in railway wagons which are run on to a tippler from whence the coal is elevated to reinforced concrete coal silos at the rate of 120 tons per hour. The same tippler is also used for discharging gypsum in bulk, a by-pass conveyor being provided for this purpose.

Grinding

The grinding department of this works is a spacious building combining both the raw and clinker grinding mills. The building is divided by a partition, on one side of which are the high and low tension switchboards together with the reduction gears and motors, which are fitted to all the mills. A slow-speed shaft for each mill projects in through the wall into the grinding room proper, in which are also placed the pumps for transporting both the slurry and the finished cement (Note 10).

Cement Mills

These mills (two in number) are similar to the raw mills of 36 ft. length and 7 ft. 2½ in. diameter, but are fitted with 750-HP auto-synchronous motors working at 3,000 volts. From the cement mills the cement is transported to storage by a pneumatic system through a pipeline 336 ft. long and 4 in. in diameter (Note 11). The vertical height to which the cement is elevated through this pipe to the silo is 73 ft. 9 in., and four rotary compressors, each having a cubic capacity of 525 ft. at 40 lbs. pressure, provide the necessary power for the system.

The cement from the mills runs into one or other of two tanks fitted with a float valve which is operated by the level of the cement in the tank. The release of this valve admits air into the tank, which causes the cement to be projected into storage; meanwhile the other tank is being filled in similar manner.

Hope 10 Figure 10. 3-spout Fluxo packer.

Hope 9 Figure 9. Main switchboard and 3 / 4 kV Transformers.

Cement Storage

Six reinforced concrete silos, each of 1,500 tons capacity, are provided, one being divided into compartments for special grades of cement in small lots. Packing is done automatically, involving the use of valved bags. These bags are hung on the delivery spout of the weighing machine, and when the correct weight of cement flows into them they are automatically discharged from the machine and fall down a chute ready for loading into railway or road vehicles. Above the weighing machines is a special cement storage hopper fitted with mixer arms after the manner of a slurry mixer. A slight and continuous injection of compressed air to the hopper renders the cement of a fluid nature and enables it to flow freely by gravity into the bags.

Power Supply

For the purpose of providing power to the factory the supply area of the Yorkshire Electric Power Co., Ltd., was extended by the Electricity Commissioners into Derbyshire, to include the village of Hope (Note 12). An overhead ring line working at 33,000-volts pressure has been extended from the neighbourhood of Sheffield, and in the event of failure on one line the alternative route could be used to maintain the power supply. Motors exceeding 150 HP are run at 3,000 volts, while 400-volts pressure is available for motors of 150 HP and less. The distribution of the power is accomplished through the medium of four sub-stations. At sub-station "A" two 3,000-kVA transformers and switchgear are provided with facilities for extension to 9,000 kVA. In this sub-station the pressure is stepped down from 33 kV to 3 kV and the lay-out provides for the supply of power and lighting current to the district generally.

Sub-station "B" contains the two metering boards (one the property of the Power Company and the other the property of Messrs. G. & T. Earle, Ltd.) on which are fitted recording instruments to provide a continuous record of units consumed as well as a kVA meter which records the maximum demand in kilovolt-amperes. This instrument comprises a watt-hour meter and a reactive component meter mounted in the same case and coupled together by a special system of gearing in such a manner that a true integration of kilovolt-ampere hours is obtained. This meter is guaranteed accurate at all power factors from unity to zero, both leading and lagging.

Maximum demand is ascertained on the Power Company's panel by means of a thermal type indicator. In this instrument the ingoing supply is utilized to heat the air in a differential thermometer tube. The consequent expansion of the air in the bulb pushes a liquid over into a reading tube provided with an indicating scale. The amount of liquid so displaced remains in the reading tube and represents the maximum demand until the instrument is re-set.

In addition, this sub-station provides for the distribution of the power with appropriate switches to all parts of the works, and transformers stepping down to 400 volts for the smaller motors and 230 volts for lighting are here provided.

There is a further subdivision from sub-station "B" into stations "C" and "D", the former of which is situated near the quarry and provides power for the excavator, air compressor and well drills as well as for a motor generator which converts the 3-phase supply to 250 volts DC for use on the electric locomotives engaged in hauling the rock from the quarry face to the crusher house. Sub-station "D" is situated in the clayfield and provides power for the washmill, slurry pump and motor supply.

The works generally have been built in a substantial manner with concrete blocks made of local limestone and cement from the factory of Messrs. G. and T. Earle, Ltd., at Wilmington, and a pleasing grey colour in harmony with the surroundings is obtained. The office block contains the chemical laboratory and testing rooms as well as provision for the Works Manager and his staff, while a visitors' dining room and garage adjoin. All buildings are of fireproof construction and practically no woodwork, other than furniture, is to be seen in the factory. With minor exceptions the works have been planned throughout and the machinery and buildings erected by Messrs. G. & T. Earle's own staff.

The electric navvy is by Ruston & Hornsby, Ltd.; electric locomotives by Metropolitan-Vickers, Ltd.; jaw crusher and clay washmills by Vickers-Armstrongs, Ltd.; gyratory crusher by Symon Bros.; combination mills, pneumatic cement transport, kilns, and bag-packing by F. L. Smidth and Co., Ltd.; motors for combination mills by Crompton-Parkinson, Ltd.; slurry screen by Sunderland Forge & Engineering Co., Ltd.; dust-collecting fans by Keith, Blackman & Co. (Note 13); coal-wagon tippler by Mitchell Conveyor and Transport Co., Ltd.; electrical apparatus and instruments by Geo. Ellison, Ltd., Metropolitan-Vickers, Ltd., Reyrolle & Co., Ltd., Crompton-Parkinson, Ltd., and Nalder Bros. & Thompson, Ltd.; underground cables by British Insulated & Helsby Cables, Ltd., and MacIntosh Cable Works Co.; drag-line scraper by Mr. E. F. Sargeant.

The pamphlet, issued to visitors given guided tours during the early months of the plant's operation, although less technical in tone, provides considerably more detail. The author was not keen on punctuation; in the interests of readability, this has been remedied.

Earle's Cement Works at Hope

INTRODUCTION

There is much to be said for and against the selection of the Hope Works as a centre to which to take anyone who wishes to see how Portland cement is made.

From the point of view of demonstrating how scientific is the process of manufacture of this most valuable building material, no other plant could be more suitable. But the Hope Works are situated in the heart of the Derbyshire Peak district, and no matter how interesting the manufacture of Portland cement may be, the beauty of the surrounding country forces itself upon one's attention. If at the end of a day's inspection the visitor to Hope feels that he does not know as much about the making of cement as he ought, we will gladly forgive him and trust that the following brief description will help him to recall the various processes which he will have been shown.

It has been said by one writer describing the Derbyshire Peaks and referring to the fact that industry is gradually encroaching upon several of the recognised beauty spots that "engineering science has so many other things to consider that it patronises aesthetics only when it is in the mood, not otherwise". May we point out that the preservation of the landscape and the beautiful surroundings of Hope has been considered of cardinal importance in the entire scheme of construction, and every advantage has been taken of the contours of the land to make the works as unobtrusive as possible?

PRELIMINARY WORK

Before describing the Works there are several ancillary schemes in connection with their construction to which we should like to refer.

The site of the Works is nearly a mile from the village of Hope and originally the only possible means of reaching it was by travelling over a rambling and picturesque old cart track—quite inadequate for carrying the heavy lorries which form part of the transport service to the neighbouring towns of Sheffield and Manchester, etc. (Note 14)

When the question of the provision of the new road came to be discussed there was naturally only one type of construction which suggested itself as the most satisfactory one to adopt for exceptionally heavy traffic—the all-concrete road.

The road, which commences by the river bridge close to St. Peter's Church, Hope, is of two course construction; the bottom course, which is reinforced, is 6 inches thick composed of 4½ parts crushed limestone, 2½ parts sand to one part of "Pelican" Brand cement, whilst the top course is 2 inches thick and composed of 3 parts Penmaenmawr granite, 1½ parts of sand to 1 part of "Pelican" Brand cement.

At a short distance from the village the road has a gradient of 1 in 9 and for the remainder of its length to the junction of the Pindale Road the average gradient is 1 in 40.

The carriageway is 18 ft. wide, and laid directly on to the concrete surface at each side are six-inch pre-cast concrete kerbs. The first thousand yards of the road have been laid under the direction of the Chapel-en-le-Frith R.D.C. (Note 15), whilst for the remainder of its length it is a private works road.

With regard to rail transport, it was necessary first of all to construct a branch railway between the site and the Dore and Chinley branch (Note 16) of the L.M. & S. Railway. The distance between the two points is nearly 2 miles and a total length of 7,000 yards of railway sidings had to be constructed.

It is interesting to note that in order that the newly cut embankments should not obtrude on the landscape they were sown with grass seed immediately the work of excavation had been completed.

To carry the railway to the site involved the construction of a viaduct over the Edale Road and the River Noe, a bridge over the main road from Sheffield to Manchester via Chapel-en-le-Frith, and also two smaller bridges. The viaduct consists of 8 spans, it has a total length over piers of 345 ft., the two centre spans being 58 ft. 6 ins. clear, and, in accordance with modern practice, the centre pier is a double one with an expansion joint down the centre which allows any movement due to varying weather conditions to take place without unduly stressing the structure (Note 17). The bridge is 117 ft. long and has a main span of 54 ft. which is sufficient to accommodate future widening at this point.

These structures are of reinforced concrete and in their design consideration was given to the use of the local limestone as aggregate. Hitherto important reinforced concrete structures in the district have been built with granite or basalt concrete, but it was considered that the merits of the crystallised limestone of the Carboniferous beds should be investigated. Preliminary tests proved beyond doubt that 6 to 1 concrete with limestone as the aggregate and a modern high quality cement such as "Pelican" Brand was more than sufficient in strength. Further investigations as to the possibility of chemical change in the aggregate after a lapse of time were also reassuring, and the work proceeded using limestone obtained on the site and quarried in the ordinary course of preparing the new limestone face for cement manufacture.

<There followed a long excursion on concrete mix design, not relevant to this site.>

GEOGRAPHICAL ADVANTAGES OF HOPE WORKS

The firm of G. & T. Earle Ltd., which possesses four works in the Hull district, was founded in Hull in 1809 (Note 18).

Earle's Cement is known to every architect, engineer and builder in the North of England and, indeed, in the Midlands there are very few who are not familiar with the famous brand of cement which is contained in the sack which has a pelican for its "guardian".

In order to give the best possible service to customers in South Lancashire and South Yorkshire, it was decided to erect a works in the centre of industrial England, and after a careful study of the geology of several districts it was found that at Hope there were exceptionally good raw materials.

RAW MATERIALS

Portland cement can be produced from any suitable materials containing the necessary constituents, which are lime, silica and alumina. The raw materials are usually carbonate of lime in the form of chalk or limestone, and silica and alumina in the form of clay or shale.

The two necessary materials are not always found upon the same site, but at Hope this fortunately is the case and the plant is situated between and adjoining supplies of limestone and clay which are almost inexhaustible.

The manufacture of cement may be divided roughly into five stages:

  1. Winning of raw material
  2. Breaking down and intimately mixing the raw materials with water (Note 19)
  3. Burning this mixture (called "slurry") into hard clinker
  4. Grinding the clinker to a fine powder
  5. Storage, packing and despatch.

LIMESTONE

To the south west of the Works is a large hill of limestone (Note 20). The foot of the hill is immediately behind the kilns and it rises to a height of 500 ft. above the level of the Works. The known depth of the limestone below ground level is 2,000 ft. so that at the summit of the hill there is a depth of at least 2,500 ft. of stone available for quarrying.

A method of quarrying new to this country has been adopted, that is, instead of working into the face of the stone in terraces, the stone is taken from the summit in horizontal slices of about 60 ft. deep and in this way the hill will be gradually lowered.

The blasting operation consists of inserting explosives into deep borings which are connected by an instantaneous fuse and electrically fired. By this means it is possible to blast 1 million tons of stone in one operation and the method is so efficient that practically no secondary blasting is necessary since all the loosened stone is less than 4 ft. cube. The loose stone is afterwards picked up by an electrically operated navvy on caterpillar wheels which is capable of raising 6 tons in one bucket-load. This discharges the stone into tip wagons which are hauled by electric locomotives to the main crusher house.

Here the stone is tipped into the largest jaw crusher that has been made in this country. It has two massive ribbed jaws, one fixed and the other swinging, and is designed to crush blocks of stone up to 4 ft. cube, and weighing approximately 5 tons down to small pieces of 6 in. cube and but a few pounds in weight (Note 21).

This crusher is placed near the summit of the hill and on the same level as the quarry floor. It will be readily appreciated that it was no mean task to lift such a gigantic piece of machinery, which weighs some 150 tons, to its position nearly 400 ft. above the works' level. The largest section lifted at one time weighed 25 tons.

From the jaw crusher the stone is carried 350 ft. by a belt conveyor to the cone crusher—a smaller type of machine which reduces each piece of stone from 6 in. down to ½ in.

From the cone crusher the stone is conveyed by two belt conveyors, one 60 ft. and the other 500 ft. long, to storage bins which are erected immediately behind the raw materials grinding mills.

CLAY

The clay, which consists of decomposed shale formed during the past centuries, and also of an alluvial deposit which has gradually worked down from the higher ground (Note 22), is situated on the opposite side of the works from the limestone quarries. This clay has a silica ratio which provides an excellent material for cement manufacture —particularly for rapid hardening Portland cement which has so revolutionised ideas on speed of construction in building work during the past few years.

The first site to be worked is 12 acres in area and the clay is 12 ft. in depth. It is procured by means of a drag-bucket, with an opening 7 ft. wide, which is dragged over the ground. Its effective working area is 850 ft. and as much as 4 tons can be picked up in one scrape.

After excavation the clay is tipped direct from the scraper into wash mills where it is liquified by the addition of water and converted into clay "slip" at the rate of 60 tons per hour. This fluid clay is then pumped to the two storage tanks which are situated close to the grinding mills. Each tank holds about 620 tons of "slip" (Note 23).

GRINDING RAW MATERIALS

From the limestone storage bins and from the clay slip tanks accurately proportioned quantities of both materials are brought together in the wet grinding mills. There are two of these steel ball mills each 37 ft. long and 7 ft. in diameter. So finely are the materials ground together that when they pass out of the mill in the form of slurry practically all of it will pass through a sieve of 32,400 holes per square inch (Note 24). A sieve of this size has a mesh which is finer than the mesh of silk. The mills deal with 42 tons of slurry per hour.

SLURRY TANKS

Centrifugal pumps convey the slurry from the grinding mills to the slurry storage tanks which are about 150 ft. distant. There are five tanks, each 30 ft. in diameter and 35 ft. deep. In these the slurry is kept continuously in motion by means of compressed air mixing arrangements through fixed pipes in the bottom of each tank. Each mixer holds sufficient slurry to make 300 tons of clinker.

It is possible to regulate the chemical composition of the slurry by mixing the contents of any of the tanks with any other tank, as each tank is provided with an outlet into either of the other four tanks.

The tanks are situated on the slope of the hill and in such a position that the slurry gravitates from them into the feed ends of the rotary kilns (Note 25).

ROTARY KILNS

Now comes the third stage in manufacture, which consists of evaporating the water present in the slurry and gradually heating the dry material thus obtained to a temperature of about 2,800 degrees Fahr. (Note 26) to effect the chemical combination necessary to produce the cementitious properties of the material.

It is perhaps in this process of manufacture that the greatest improvements have been effected. A century ago, in Aspdin's time, the raw materials were burned in a lime kiln and after the lime kiln, special kilns were devised such as the bottle and chamber kilns which were loaded with slurry, fired, and, after the calcination was completed, allowed to cool when the burnt material was drawn. Then came the rotary kiln, which is a slightly inclined steel cylinder which is gradually rotated whilst burning is proceeding, the speed of rotation being about one revolution per minute. The slurry is fed continuously into the kiln and moves by gravitation from one end of the kiln to the other.

The fuel consists of finely ground and thoroughly dried coal which is introduced into the lower end of the kiln by a jet of air issuing from a blast fan. In the lower third of the kiln an intense heat is generated by the combustion of the finely ground coal.

So far two kilns have been installed at Hope Works. They are each 289 ft. long by 10 ft. in diameter and when loaded weigh 651 tons.

Advantage has been taken of the suitable contour of the ground on which the Works are situated with the result that the kiln-house floor is parallel to the required slope of the kilns. The kilns are driven by electric motors direct coupled to reduction gears.

The coal which is used is railed to the Works from the neighbouring collieries in Derbyshire, Lancashire and South Yorkshire. The trucks are tipped bodily into a receiving hopper and conveyed thence by an electric elevator and belt to the coal silos erected near the grinding mills.

The fuel is pulverised by mills, which are the most up-to-date yet introduced, housed at the firing end of the kilns.

COOLING THE CLINKER

Each of the kilns embodies a cooling system. This consists of a set of 12 cylinders each 4 ft. in diameter and 20 ft. long placed around the discharge end of the kiln, the centre line of the cylinders being parallel to the centre line of the kiln. The hot clinker leaves the kiln shell at its extreme end and is discharged through 12 holes on its periphery into each of the 12 cooler cylinders. In each of these the clinker is slowly transferred to the discharging end where it falls on to a belt conveyor and is carried to one of the hoppers on the kiln side of the clinker store.

CLINKER STORE

The clinker store consists of an open concrete bin capable of storing 3,850 tons of clinker. An overhead travelling crane grabs clinker from either of the two clinker hoppers and delivers it to the store or into the grinding mill hoppers. By this system it is possible to make any mixture of clinker that may be desirable.

GRINDING MILLS

The clinker is ground in two combination grinding mills which are installed in the milling house parallel with the wet grinding mills, and are of exactly the same size as the wet mills. These mills are divided into compartments. The first compartment into which the clinker is delivered is charged with steel balls 3½ in. to 2 in. diameter. The coarse grit from these compartments passes through a slotted diaphragm into an intermediate compartment where it is further reduced by balls of 1 in. diameter, and then passes to the final stage where it is reduced to an impalpable powder by smaller grinding media. The total weight of steel balls in each mill is 50 tons.

STORAGE SILOS

The finished cement is then delivered a distance of 200 ft., by means of compressed air, to a battery of 6 storage silos.

Each silo is 70 ft. high and 20 ft. in diameter and has a capacity of 1,500 tons (Note 27). One of the silos is sub-divided into bins in order to store cement to comply with customers' requests when cement to a special specification is required.

PACKING

Packing is done automatically, involving the use of valved bags. These bags are hung on the delivery spout of the weighing machine, and when the correct weight of cement flows into them they are automatically discharged from the machine and fall down a chute ready for loading into railway or road vehicles. Above the weighing machines is a special cement storage hopper fitted with mixer arms. A slight and continuous injection of compressed air to the hopper renders the cement of a fluid nature and enables it to flow freely by gravity into the bags. Each packer can fill and weigh 600 1-cwt. bags per hour.

TESTING FACILITIES

The manufacture of cement at these Works is under close technical control from beginning to end and is checked at every stage. The clay is sampled in the storage tanks; the limestone is sampled in the silos before entering the grinding mills. Slurry is tested before entering the slurry tanks and also before entering the kiln, whilst continuous samples of the finished product are taken as it enters the storage silos and while it is being packed.

A very completely equipped laboratory has been erected on the Works where a number of trained chemists are continuously employed.

POWER

The electricity to run these Works is being supplied by the Yorkshire Electric Power Company. It is conveyed to the Works by two overhead power lines from the Company's Power Stations at Barugh and Ferrybridge, near Barnsley (Note 28).

The duplicate 33,000 volt lines in the vicinity of the Works are supported by reinforced concrete masts, specially designed with a view to obtaining an attractive appearance. The amount of electricity consumed by the Works is approximately 5 million units per year (Note 29). On arrival at the Works the current is transformed down to 3,000 volts by two transformers and then to 400 volts, which is the pressure used to run the smaller sections of the plant. The two 3,000 / 400 volt transformers are in the main motor house which has been constructed at the discharge end of the grinding mills and curtained off from the mills by a concrete wall. The room contains the motors for running the mills, and also all the air compressors, vacuum pumps and the main switchboards.

WATER SUPPLY

A difficulty at first was experienced in obtaining an efficient supply of water since, when borings came to be made, it was found that the site of the Works was actually the site of an extinct volcano and no matter how deep a well was sunk it would be impossible to reach water. Water is, however, procured a little way from the site by means of a bore-hole 500 ft. deep and 15 in. in diameter and is pumped to the surface by compressed air. An alternative supply is a well 80 ft. deep and the water in this case is brought to the surface by ordinary centrifugal pumps.

GENERAL

It is possible to manufacture 3,200 tons of Portland cement per week at Hope, which brings the total weekly output from all our works to 10,000 tons. A special feature of these Works is that in their construction everything possible has been carried out in concrete. Indeed, with the exception of glazed brickwork and the brick linings in the kilns, there are no clay bricks on the Works. Neither is there any corrugated iron since asbestos cement sheeting has been used for the roof and wherever sheeting has been necessary.

The clinker stores, silos, tanks and the 150 ft chimney are of reinforced concrete, while the remainder of the buildings which include the mill house, offices, garage, stores, workmen's canteen, etc., are built with concrete blocks.

These 18 × 9 × 4½ in. blocks are composed of limestone aggregate with a backing concrete mixed in the proportion of 8:1 while the face is in the proportion of 5:1. All the blocks have been manufactured on the Works' site and over 5,000 bocks per day for the past 18 months have been produced on one machine. For decorative effect, string courses and quoins of rock-faced blocks made in moulds copied from actual blocks of limestone have been used.

It is a fact that the effort which has been made to ensure that the buildings harmonise with their surroundings has met with success.

Everything possible has been done to make Hope Works the most up-to-date in the world. Apart from conveyor belts in the Works there are no belt drives, since all the machinery is driven by motors direct coupled to reduction gears. Centrifugal pumps are provided for the slurry, the conveyance of finished cement is pneumatic, and the only elevator is that used for filling the coal store from the railway tracks.

The dust problem which always has to be faced in cement works has received very special attention; collecting pipes have been connected to every point from which dust likely to be produced, and thus the Works are rendered practically dustless.

NOTES

Note 1: G & T Earle was a subsidiary of BPCM. Its absorption into the administrative structure of Blue Circle was delayed by the setting up of a satellite office in Hull, around which a little empire evolved, drawing in Wilmington, Humber, Hope, Barnstone and Kirton Lindsey.

Note 2: Gyratory crushers had been used for coarse crushing for 22 years, the first probably being the one at Southam.

Note 3: Hope was rare among Blue Circle plants in that it was progressively expanded. The FLS layout of kilns and mills left room for additional units to be added on, but eventually the free space ran out and the plant became somewhat congested. This was relieved by the construction of the dry process kilns (1970) on a separate spacious site.

Note 4: The use of Cardan shafts allowed all gears and motors to be kept outside the dusty atmosphere of the mill house. The system was only possible with the FLS Symetro gear-box, which could deliver the very high torque necessary. This system was first used here and at Ketton and West Thurrock earlier in 1929.

Note 5: At the typical 39.5% moisture content of the time, 17,000 ft3 contains 470 t of dry raw material, equivalent to about 15 hours run on two kilns. The inadequacy of blending and storage capacity was not characteristic of FLS process design, and was probably mandated by BPCM. Sensible storage was subsequently added during the late 1930s.

Note 6: The limestone, clay slip and water were all metered to the mill volumetrically, and were adequate to control fineness, carbonate content and moisture content respectively.

Note 7: The real dimensions were 84.2 m long (82 m from the cooler ports) by 2.550 m, with burning zone 28.75 m by 3.150 m. 28.75 m is 94' 3.9": the 46' given is an inexplicable error. The pictures clearly show the expanded burning zone extending nearly to the third tyre. The shell sections are each 2.4 m long. The basic design - a simple tube with a burning zone expanded by 0.6 m, and a 12-tube planetary cooler - was a variant of the FLS design also installed at the time at Bevans, Ketton, Swanscombe and West Thurrock. See the description of the Ketton kiln.

Note 8: Again, the inadequate storage was a BPCM design. The much smaller Ketton had a full-sized clinker store. The poor storage, with little room to expand, was finally resolved in 1938 with the construction of an overhead-crane store.

Note 9: The Ketton installation had a separate coal drier, and fine coal was conveyed to storage by elevator. The use of the mill here in air-swept mode may have been based on experience at Humber; the coal driers there had been abandoned at an early stage.

Note 10: The accommodation of rawmills and finish mills in a common mill house became an established feature of FLS plants. It allowed a rationalisation of civil engineering, feed material handling (through a common crane store), services and control. Oddly, it was not done at Ketton, but a common mill house, extendable at both raw and finish ends, became a central part of the design of hard-rock wet process plants at Ribblesdale, Southam, Drogheda, Limerick and Padeswood. Hope seems to have been the first. As mentioned, the raw and finish mills were of identical dimensions. With the installation of the dry process in 1970, the wet rawmills were converted for cement milling as a cost-saving measure.

Note 11: Fuller-Kinyon pumps had been used elsewhere, beginning with Bevans, but this was FLS's own Fluxo system.

Note 12: Hope might have been low on the list of remote settlements for electrification had it not been for the construction of the plant.

Note 13. The full company name was James Keith and Blackman Company - it was changed to Keith Blackman Ltd in 1937.

Note 14: Originally a track ran through the valley from Pindale to Bradwell.

Note 15: Rural District Council. Chapel-en-le-Frith Rural District occupied most of the High Peak part of Derbyshire.

Note 16: Constructed 1894 as an alternative Sheffield-Manchester route.

Note 17: The viaduct was subsequently replaced with a prestressed concrete structure.

Note 18: The four works were Wilmington, Humber, Barton and Stoneferry. The latter two (it fails to mention) were closed as soon as Hope was up and running. G & T Earle, although founded as merchants in 1809, did not make Portland cement until 1875.

Note 19: There was evidently not the slightest prospect of considering the possibility of dry process. If a dry process had been selected, during the period 1929 to 1970 (in which the plant made 16.65 million tonnes of clinker and used 123.6 million GJ of energy in the form of coal), about 50% less fuel could have been used, and the emission of 5.7 million tonnes of carbon dioxide avoided.

Note 20: This was Nun Low. It was already raddled with centuries of lead mine workings, and was more recently in use for lime and roadstone.

Note 21: The jaw crusher was later replaced with a 54 inch gyratory crusher.

Note 22: The valley floor alluvium and boulder clay were eventually used up, and the underlying Bowland Shale was used.

Note 23: This implies that the slip contained about 62% moisture.

Note 24: The 180 mesh sieve of the time had an aperture of 96 μm.

Note 25: On most plants, spoon feeders were fed by pumping from a tank at a lower level, at a flowrate in excess of that needed. The excess slurry in the spoon feed sump overflowed a weir and returned to the storage tank. The weir maintained the slurry level in the sump. Here, as with supply of clay slip to the rawmills, the spoon feeders were fed by gravity from above, so no overflow was possible, and a control loop was needed to maintain a constant level in the sump.

Note 26: This is 1538°C, which is an absurdly high estimate. Hope's easy-burning material probably required 1400°C (2552°F) or lower.

Note 27: This is wrong: the silos were - and still are - 30' in diameter.

Note 28: In 1929, power supply still consisted of central power stations with radial distribution lines. "Grids" with greater connectivity began to be set up on a local scale in the early 1930s, and the National Grid, linking all regions, was finally connected up in 1938.

Note 29: If the plant makes its rated 160,000 tons a year, then this represents an enviable power consumption of 31 kWh per ton. Of course, the real power consumption was about three times this amount.

Note 30: