Cement Kilns

Wilmington

Earles LogoEarle's Pelican Brand.

Location:

  • Grid reference: TA09973041
  • x=509973
  • y=430413
  • 53°45'31"N; 0°19'55"W
  • Civil Parish: City of Hull, East Yorkshire

Clinker manufacture operational: 1875-1969

Approximate total clinker production: 8.7 million tonnes

Raw materials:

  • 1875-1899 chalk ballast, River Hull Alluvium from 510400,430800
  • 1899-1909 chalk from Halling Manor, Humber Alluvium from Barton Ings
  • 1909-1913 Upper Chalk (Seaford Chalk Formation: 85-88 Ma) from Globe (Greenhithe) and hard Middle Chalk (Welton Chalk Formation: 90-94 Ma) from Leggott’s Quarry, South Ferriby, Lindsey 500000,421700, and alluvial clay from Killingholme, Lindsey 516550,419750 by barge (13 km)
  • 1913-1969 alluvial clay from Barrow on Humber, Lindsey 505100,423400 by barge (10 km): hard Upper Chalk (Burnham Chalk Formation: 85-90 Ma) and Middle Chalk from own quarries by rail to a common crusher/silo installation in Hessle (501740,425605), loading main line trains for 10.4 km trip to the plant: quarries at:
    • 1913-1952 Hesslewood Quarry, Hessle, ER 501950,425850
    • 1926-1969 Humberfield Quarry, North Ferriby, ER 501300,426100

Ownership:

A Roman Cement plant - ownership unknown - had existed here in the 1850s and is shown on the 1856 map. Earle’s had been making Roman Cement at a site on the Humber bank (at 508700,427700) since 1821. They first claimed to make Portland cement at that site in 1857, but this product was just a modified Roman cement. The company acquired the Wilmington site with the adjacent land south of the railway in 1866, and the Humber bank plant site was sold to the Hull Dock Company. Three kilns were set up for Roman cement production at the new site. These were small kilns, making together 45 t/week. A fourth was added in 1869, and production of Roman cement peaked in the early 1870s at around 3000 t/year. The Roman kilns were progressively turned over to Portland from 1877 when Roman cement sales started to drop dramatically. Two remained open (without bottle extension) as part-time “Roman” kilns until 1907, although from 1898 there were only two or three Roman cement burns per year. They were then converted into silos.

True Portland cement production began around 1875 with three bottle kilns (122 t/week ) and three more (122 t/week) were added in 1876. In 1882, a seventh (41 t/week) was installed and two of the Roman kilns were provided with bottle extensions, providing a further 54 t/week. The other two Roman kilns, left open, were also available most of the time for Portland, and could provide 41 t/week. This added up to a final bottle kiln capacity of 380 t/week. In 1888, eight Killick kilns were installed, yielding 461 t/week. In 1895, eight Batchelor kilns (208 t/week) were installed and in 1898, twelve Hilton kilns (311 t/week) were installed, bringing chamber kiln capacity to 980 t/week. The surplus dryings of the chamber kilns were used to feed the bottle kilns, allowing removal of the original separate drying flats.

One of the bottle kilns was converted in 1900 into a Schneider-type continuous kiln, output 80 t/week. Further developments were done in concert with the conversion to "local" (i.e. hard) chalk supply, discussed below. In 1906, rotary kilns A1 and A2 were installed and the remaining bottle kilns and the Schneider were decommissioned. The plant capacity at this point in t/week was chamber 980 and rotary 860, giving a total of 1840 t/week. Davis’ 1907 capacity estimate was 2000 t/week. The plant’s clinker output was actually 91,450 tonnes in 1907. The Batchelor and Hilton kilns static kilns were finally cleared in 1912 in preparation for rotary kiln A3. The Killick kilns remained in operation until May 1915, after which they were demolished. During WWI, discussion continued on whether further capacity expansion should be at Wilmington or at Hope. The installation of A4 in 1920 was the immediate response to this, but the plant site was already being seen as misplaced, and from then on it became flexible, make-up capacity, with kilns A1 and A2 frequently stopped for long periods during downturns.

The plant continued into WWII, with only one destructive air strike on 17/7/1941, when the rawmills were hit (along with many houses in the adjacent streets), stopping the plant for three months . Following the 1944 downturn, the plant was shut down 7/1944-3/1946. The plant made sulfate resisting clinker alongside ordinary clinker from 1953 to 1969.

Transportation was initially by water using extensive wharfs on the River Hull. From the outset, sidings on the adjacent North Eastern Railway (originally the York & North Midland Railway Victoria Dock branch) were employed, and rail transport became dominant by the end of the nineteenth century. The site was totally cleared and is now a recycling depot and ready-mix plant.

When the plant shut down in 1969, it was an anachronism. It was the only plant (apart from Padeswood) remote from its raw materials, and A1 and A2 were the oldest and smallest kilns in operation. The Heath Robinson sketches of the plant, proudly circulated by Blue Circle, were not entirely an inaccurate representation. The plant’s longevity is a testament to the peculiar status of G & T Earle within the Blue Circle organisation.

Earle’s began in the early 19th century, in typical Hull tradition, as Baltic traders, and their marketing organisation was always more important to them than their production facilities. By 1912, they had a very efficient distribution system throughout the North, and by acquiring Earle’s, the Thames-based APCM obtained the key to an otherwise impenetrable market. At the time of takeover, Earle’s needed to expand, but were out of cash and very weak, and if they had continued independent, they might well have gone the same way as other north-eastern plants. Nevertheless, Earle’s were able to make an exceptionally good deal in the takeover, in preserving a degree of independence, and amassing a mini-empire within Blue Circle, and it thereafter consistently behaved as if it were still an independent company. The procedure of the take-over throws interesting light on this. BPCM first bought Robson’s (Stoneferry ) and Skelsey’s (Barton ). Then Earle’s bought them from BPCM using money borrowed from the BPCM sponsors. Then G & T Earle Ltd was liquidated, and BPCM bought it. Then G & T Earle (1912) Ltd was constituted as a subsidiary. The subsidiary was finally wound up in 1967, but continued in spirit until 1986 as Blue Circle’s Northern Area Office, Hull. It is significant that the last remaining (2009) Blue Circle-built cement plants are Hope , Cauldon , Dunbar and Cookstown – all “Earle’s plants”.

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

Rawmills

The original plant used washmills to wash chalk and clay together on the unloading quay. After the use of Humberside chalk began in 1909, clay landed at the quay was slurried in two 15' washmills, and the slurry was then inter-ground with the hard chalk in ball mills.

Four rotary kilns were installed:

Kiln A1

Supplier: Polysius
Operated: 10/1906-7/1969
Process: Wet: an experimental Davis Preheater was added 3/1957-1958
Location: hot end 510044,430344: cold end 510058,430373: hot end enclosed.
Dimensions: (metric)

  • Original 32.00 × 2.000
  • From 1957 32.33 × 2.000

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

  • Original 0×1700: 720×2000: 32000×2000: Tyres at 4510, 15520, 30380
  • From 1957 0×1873: 413×1873: 413×2000: 27870×2000: 29172×2305: 32334×2305: Tyres at 4578, 15646, 27318

Cooler: rotary: originally metric 10.00 × 1.000 beneath kiln: this was subsequently modified to 32’1½” long and shared with A2
Cooler profile:

  • Original 0×1000: 10000×1000: Tyres at 1845, 8425
  • Subsequently 0×1372: 4639×1372: 5553×1000: 9792×1000: Tyres at 1637, 8217

Fuel: Coal
Coal Mill: semi-indirect ball mill
Exhaust: natural draught direct to stack.
Typical Output: 1906-1929 60 t/d: 1929-1948 58 t/d: 1948-1956 66 t/d: 1957-1958 80 t/d: 1959-1969 70 t/d
Typical Heat Consumption: 1906-1929 10.6 MJ/kg: 1929-1948 7.91 MJ/kg: 1948-1956 7.37 MJ/kg: 1957-1958 5.37 MJ/kg: 1959-1969 7.37 MJ/kg


Kiln A2

Supplier: Polysius
Operated: 10/1906-7/1969
Process: Wet
Location: hot end 510040,430346: cold end 510054,430375: hot end enclosed.
Dimensions, metric 32.00 × 2.000
Rotation (viewed from firing end): ?
Kiln profile: 0×1700: 720×2000: 32000×2000: Tyres at 4510, 15520, 30380
Cooler: shared: see A1
Typical Output: 1906-1948 60 t/d: 1948-1957 64 t/d: 1959-1969 69 t/d
Typical Heat Consumption: 1906-1929 10.6 MJ/kg: 1929-1948 7.98 MJ/kg: 1948-1957 7.31 MJ/kg: 1958-1969 7.40 MJ/kg
Identical in all other respects to A1.


Kiln A3

Supplier: FLS
Operated: 5/1913 -1969
Process: Wet
Location: hot end 509856,430430: cold end 509917,430446: hot end enclosed.
Dimensions: (metric)

  • Original: 63.00 × 2.700B / 2.400CD
  • Final: 62.69 × 2.700B / 2.400C / 3.010D

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

  • Original: 0×2400: 3000×2400: 3000×2700: 10350×2700: 12375×2400: 63000×2400: Tyres at 1900, 13675, 25575, 40075, 56850
  • Final: 0×2400: 3023×2400: 3023×2759: 10439×2759: 11963×2400: 57887×2400: 59106×3010: 61925×3010: 62687×2426: Tyres at 1930, 13705, 25605, 40105, 56880

Cooler: concentric rotary metric 9.50 × 1.050 / 1.650 beneath kiln: replaced with rotary cooler 62’5”× 5’0⅞” (metric 19.02×1.450)
Cooler profile:

  • Original: 0×1200: 3640×1200: 3640×1050: 3920×1050: 3920×1650: 9500×1650: Tyre at 2150 with trunnion end bearing: Turning gear at tail end.
  • Final: 0×1545: 19025×1545: Tyres at 3607, 15900

Fuel: Coal
Coal Mill: semi-indirect ball mill
Exhaust: initially natural draught direct to stack: ID fans were added after WWII.
Typical Output: 1913-1932 166 t/d: 1932-1940 176 t/d: 1940-1948 169 t/d: 1948-1969 190 t/d
Typical Heat Consumption: 1913-1927 7.6 MJ/kg: 1927-1932 7.06 MJ/kg: 1932-1943 6.68 MJ/kg: 1943-1957 7.15 MJ/kg: 1957-1969 7.00 MJ/kg


Kiln A4

Operated: ?9/1920-1969
Location: hot end 509858,430423: cold end 509919,430439: hot end enclosed.
Dimensions: (metric)

  • Original: 63.00 × 2.700B / 2.400CD
  • Final: 62.84 × 2.700B / 2.400C / 3.010D

Rotation (viewed from firing end): ?
Kiln profile:

  • Original: 0×2400: 3000×2400: 3000×2700: 10350×2700: 12375×2400: 63000×2400: Tyres at 1900, 13675, 25575, 40075, 56850
  • Final: 0×2400: 2718×2400: 2718×2759: 10135×2759: 11659×2400: 57582×2400: 58801×3010: 61544×3010: 61544×2400: 62840×2400: Tyres at 1625, 13400, 25300, 39800, 56575

Typical Output: 1920-1932 162 t/d: 1932-1941 176 t/d: 1941-1947 167 t/d: 1947-1969 185 t/d
Typical Heat Consumption: 1920-1927 7.6 MJ/kg: 1927-1932 7.14 MJ/kg: 1932-1954 6.79 MJ/kg: 1944-1957 7.19 MJ/kg: 1957-1969 6.86 MJ/kg
Identical in all other respects to A3.



Sources: Cook, p 57: Francis, pp 223-225: Jackson, pp 266, 279, 302: Pugh, pp 12, 19, 28, 53, 55-64, 103, 137: J. R. Heathcote, Earle’s cement, Humberside College of Higher Education, 1988, ISBN 1870001265: The Making and Testing of Portland Cement and Concrete, G & T Earle, 1925



Old Maps

Wilmington Detail

Approximate capacity: tonnes per year
Wilmington Capacity

Wilmington 1924
A rather idealised view of the pre-rotary plant in 1900, from a letter heading.
A. - 8 Batchelor kilns
B. - 12 Hilton kilns
C. - Main power plant
D. - Roman kiln bank
E. - Finish mills - remained located here until 1969
F. - Chalk wharf and main washmills
G. - 6 large bottle kilns
H. - Stores, maintenance etc.
I. - 8 Killick kilns
J. - Clay wharf and washmills
K. - Main cement store and packing area
L. - Offices
M. - Original Roman cement plant site
Any attempt at a logical layout must have been abandoned at a fairly early stage.

Wilmington 1924
Picture: ©English Heritage - NMR Aerofilms Collection. Catalogue number 10839. A high-definition version can be obtained from English Heritage. This was taken in 1924, looking north, and shows the plant shortly after the completion of the post-WWI expansion, after which very little more was done to the plant. The wharf in the foreground, once used to bring in both chalk and clay, now just handled clay brought by barge from the south bank of the Humber. The clay was washmilled in building to the right of the stockpiles. The chalk was now received by main line rail - full chalk trucks can be seen far right - and elevated to silos in the tall building by the rail track. In the right adjacent building (behind kiln 1/2 stack) contained the rawmills in which the hard Hessle chalk was interground with clay slurry. In front of these buildings are rotary kilns 1 & 2. With the installation of the much larger kilns 3 & 4, these became reserve capacity, used intermittently, but continued in that role, in increasing dilapidation, until the plant closed in 1969 - they were the last of the many early Polysius 30×2 metre kilns to operate. The larger kilns 3 (north) and 4 (south) were crammed into the northwest corner of the site after demolition of the bank of Hilton kilns previously there. The power plant (in front of kilns 3 & 4) was still operating.

Wilmington kilns
Feed ends of kilns 3 (right) and 4, around 1921. The slurry mixers between the kiln piers were a common feature of FLS designs of the period. The slurry bucket feeders were in the canopied structure, with a slurry overflow pipe returning surplus slurry to the main mixer off-frame to the right.

This article is based on a document in the G & T Earles archive held by the Hull History Centre - catalogue number DBEL/47/34.

In the nineteenth century, the major cement producing areas in the northeast of England, centred on the Tyne, the Wear, Hartlepool and the Humber, all used chalk shipped from the Thames and Medway as their main raw material. Chalk was used as ballast on the return legs of trips carrying heavy goods - notably coal - to London, and so was available at virtually zero cost. As the cement industry grew, producers needed to find a more secure source of raw material, and contracted with individual supplier quarries in Kent and Essex. As the commercial value of the chalk became evident, and demand grew, suppliers gradually raised prices. The growing use of iron-hulled water-ballasted coal ships further closed off the supply of ballast chalk. So an industry that initially made use of a readily available waste product ended up buying the same raw material at premium prices and paying for shipping it several hundred miles. Starting as the lowest-cost manufacturers, they ended as the highest cost.

The northeast plants became victims of circumstance partly because soft chalk from the southeast was regarded as the only raw material that could be used in Portland cement manufacture. Deposits of chalk actually extend as far north as Cleveland, but the material is much harder. As explained elsewhere, it was the slow development of grinding technology that determined the rate of innovation in the cement industry. Attempts to use the hard northern chalk using the primitive methods of grinding originally used resulted in failure because excessive amounts of oversized (>150 μm) particles in the kiln feed, and so northern chalk got the folk reputation of being "no good". However, by the early years of the 20th century, northeastern manufacturers realised that they had to choose between innovation and oblivion.

The painful process of changing raw material, which was undertaken by a few of the northern plants (the others ceased operation) is exemplified by the case of the Wilmington plant in 1902. This was the plant of G & T Earle, and in 1902 had a capacity of about 70,000 tonnes a year. It was the seventh largest in England, and the largest outside the Thames/Medway area (Note 1). After using cheap ballast for many years, the plant contracted with individual quarries for commercial chalk and in 1902 were obtaining material from Hilton Anderson & Brooks' quarry at Halling. Later, they used the Globe Whiting quarry at Greenhithe. The chalk delivered price was 6/- a ton or 9/- per ton of clinker - a little over 40% of the total manufacturing cost. For plants in the southeast, the corresponding figure was a few pence.

In 1888, its local competitor Adamant had started using chalk from across the Humber at New Cliff, Barton, Lincs. Earles had obtained an option for the use of the neighbouring Leggott's quarry, and had probably started using small quantities of the hard chalk on an experimental basis. Earle's was a family firm, with most of the equity held by members of the extended family, although of them, only John Hudson Earle, the managing director, took much interest in the business. It was clear that substantial investment at least in grinding equipment would be needed, and this came at a time when most large plants were also upgrading their kilns to modern forms. Earle had the difficult task of selling a costly project to the tight-fisted family, and asked Herbert Anderson to act as a consultant.

Herbert William Anderson (1858-1949) was the eldest son of William Curling Anderson, founder member of the Hilton Anderson partnership at Faversham, and had been the manager of the Halling Manor plant when it opened. He subsequently left the company to set up as an independent consultant. For Earle's, he produced a report with four options:

  • A: supplying chalk from Barton (he calls it South Ferriby), making slurry and feeding the existing set of static kilns.
  • B: supplying chalk as A, drying and grinding to raw meal, briquetting and feeding to Schneider kilns.
  • C: supplying chalk and making slurry as A, and feeding to wet process rotary kilns.
  • D: supplying chalk as A, drying and grinding to raw meal, and feeding to dry process rotary kilns.

He then went on to make the entirely sensible (but unacceptable) point that the cramped urban Wilmington site was not the place to make cement at all.

REPORT

of various proposals for the use of

- LOCAL CHALK -

and methods of treating it on its arrival at Wilmington at the works of

Messrs G & T Earle Ltd

by

H. W. Anderson, C.E.,

Fairfield

Teddington, London

1902

Dear Sirs,

In the portion of this report bound separately (Note 2), I treated on proposal A and under which the chalk was deposited in the storage hopper at Wilmington and used to supply the wash mills in that form instead of any London Chalk.

The next on the list of proposals enumerated on page 2 of the other report is

PROPOSAL B.

This is the same as far as delivery of the ground chalk (Note 3) into storage hopper at Wilmington, and which costs as described under A 2/- per ton of chalk.

Clay is unloaded on wharf by grab (Note 4) and fed into rotary driers by barrows from the storage heap. It is then dried and passes through a pulverizer to fine powder from which it goes into a storage hopper of about 200 tons capacity near the chalk hopper.

The apparatus at the bottom of both the chalk and clay silos and into which the material falls automatically consists of a Pratt & Whitney, or other mixing apparatus which is adjusted by the chemist as often as desirable. It is not anticipated that with the small regular percentage of moisture now left in both the chalk and the clay under this process such adjustment will be necessary as the average of both materials stored and mixed in such large bulk will run exceedingly uniform and require much less attention than in their natural state.

It will be advisable to have proving silos however, to be perfectly sure all is right in case also any error by the mixing apparatus getting out of adjustment, and to ensure the most perfect quality for the cement at all times, so from this it is conveyed in a mixing conveyor and elevator into an octagon tower as shown on drawing, each compartment is capable of storing about 150 tons of material. I may say there are a large number of works where no such precaution is taken and the mixing chamber dispensed with. This was one of the points I complained of to Edison as to his Stewartsville Works (Note 5) as all his mixing appliances were to be used before the blending of the 2 materials and not after (Note 6).

These 8 compartments would probably be occupied as follows;—

  1. of these would be being filled from this trough by central elevator
  2. being emptied to feed grit mill and thence to feed brick machines.
  3. being mixed off into a fourth one for correction by other central elevator.
  4. being filled from No 3.
  5. under test.
  6. passed ready for use.
  7. with neat chalk.
  8. with neat clay.

A mixing elevator as well as the filling elevator would be in the centre compartment of these so that anyone of them could be quickly and automatically blended with any other or corrected with a small drizzle of neat clay or neat chalk as desired by the chemist from compartments 7 and 8.

This form of construction is the simplest, compactest, and cheapest possible and is quite original and unique in design (Note 7). There are louvred openings at the bottom by which the material can be seen and poked down if it ever hangs up (Note 8) by arching over inside and no moving parts are required for closing those openings.

After leaving these chambers when approved, the material passes into large size grit mill, here it is most thoroughly further blended and incorporated and ground to the fineness desired and on leaving which it passes into a conveyor to feed the hoppers of 6 brick machines. The hourly output of these would treat material equal to about 2 cement tons perhaps, so it would be necessary to have 6 of them running night and day (Note 9).

For these a trifling percentage of water is added to that already in the material say 7% total, and compressed into bricks. These are then stacked on brick trolleys and run off to the lifts to feed the Schneider and open kilns in the condition they are and the operation is complete.

If Humber Clay has 45% of moisture (Note 10) in it to be expelled before it can be ground and 1030 tons (Note 11) of the moist clay is required weekly to produce 1600 tons of cement, this will contain 465 tons of water, and require @ 5 lbs water from 1 lb of fuel (Note 12), 93 tons of coal to dry it with 2 rotary driers running 5½ days night and day or say 130 hours apiece should just manage this quantity and so there is no margin over. It will be advisable to provide a third in case of repair stoppage, or overwork of the other 2 from damper material, but if there is always less moisture than 45%, it is probable 2 driers would be enough for the work.

The value of 93 tons of coal for three driers at say 10/- on wharf equals on 1600 tons cement say 7 pence per cement ton.

The fuel and labour credit for Motive power whether by gas engine, electric power, or steam has to be added.

This could doubtless be supplied by the wash mill engine which would not be required for its old work if this scheme of manufacture was adopted.

Plant in connection with driers, fan, and conveyor say20 IHP
Plant in connection with pulverizer35
Silo conveyor and mixing elevators10
Grit Mill70
Conveyor and brick machine.35
Contingencies.20
Total200

200 x 4 lbs coal per hour (Note 13) for 130 hours weekly
equals 46 tons fuel @ 10/- = £23
1 driver & 1 stoker @ £2 each night and day shifts. = £8
Oil, grease, stores &c say £2
Total £33
This equals on 1600 tons 5d per cement ton.

The Labour for all the above process may be summarised as follows:-

2 men wheeling in clay from wharf storage heap and feeding driers at rate of 8 tons per hour. 2 at night. 2 for day @ £2 weekly each.£8
1 man stoking driers night and day.£4
1 man attending motor for turning fan and seeing to material leaving the driers into hopper of the pulverizers and into which 5 tons of the dried clay would be fed hourly night and day @ £2 weekly,£4
1 man night & day attending the mixing weighers under chalk and clay silos and conveyor and elevator therefrom to octagon tower chambers and using mixing off elevator when ordered by chemist whose orders he would be under and also attending shoots @ £2 each into grit mill.£4
1 man attending grit mill, and feed therefrom into brick machine hopper 1 night and 1 day @ £2£4
1 man attending each brick machine night and day 12 men @ £2/10/- each£30
3 lads, night and day supplying trucks to same @ £1. weekly each£6
Total£60

This equals for a 1600 cement ton output say 9d per cement ton.

In actual practice of course all the above rates would be based at piecework rates, and which would run out, on average, probably slightly below above estimate (Note 14).

The labour in connection with the 17 Schneider kilns then consists of receiving the loaded brick trolleys from the lifts on upper staging. The lads attending the brick machines having put them in the lift below, 3 lads above one to each lift to run them when required and one mate to each to help unload.

6 lads night & day @ £1 each.£12
3 men bringing in fuel below to lifts night & day @ £2£12
1 burner & mate to each pair of kilns @ £2 and 30/- each weekly, night and day = 16 sets @ 70/- £56

This for 1600 ton output = 1/- per ton (Note 15).

The cost of drawing the clinker will be the same as now, probably less, as the men do not have to water the kilns at all (Note 16), and they will be nearer the clinker mills, that is 5.7 pence per ton.

FUEL With 3½ cwt coke per ton of clinker (Note 17) @ 10/- per ton = 1/9 per cement ton.

KILN REPAIRS. A charge of £10 per week for labour and material for keeping the 17 Schneider kilns in repair, or £520 per year should be enough. This is met by 1½d per ton of cement.

DRYING, MIXING AND BRICK PLANT REPAIRS. It is impossible to really say what this would run out to. If £40 weekly (equals over £2000 per year) will cover it, which it should, this will run at 6d per ton.

DEPRECIATION. If 5% over the whole Wilmington outlay including kiln plant were charged, it would be too much on some & not enough on other parts of it, but would probably form an approximate & fair amount on an average £23,500 @ 5% p.a. = £1175 equal to 3.40d per ton.

INTEREST. 5% as usual on the whole will be charged & equals same as above 3.40d per ton.

COST OF CLAY. This will be the same as incurred before in 1902. Take it at say *** (Note 18) delivered on wharf, equal to 1/4 per cement ton.

DETAILS OF ROUGH AND VERY APPROXIMATE ESTIMATE OF OUTLAY REQUIRED UNDER PROPOSAL "B".

££
Ferriby plant (as under "A")12,00012,000
Lighterage plant (optional)10,00010,000
WILMINGTON PLANT
1 hanging discharge elevator with motor and balanced bracket arm say,600
1 elevator therefrom to hopper with conveyor,500
Chalk storage hopper say,1,900
Weighing machine and shoots,300
3 rotary driers and stage and fan,1,850
Inclined clay conveyor to ditto,150
1 conveyor and 25ft elevator,100
1 pulverizer and hopper over,600
1 75 (ft) elevator to clay hopper (5 tons),100
1 clay storage hopper,200
1 weigher and shoots &c,200
82 ft spiral to octagon hopper,150
1 octagon hopper in cement and iron,1,800
1 90 ft filling elevator 20 ton capacity,120
1 90 ft mixing elevator (50 ton capacity),180
Conveyor to tube mill 45 ft. 12 ton,100
1 large size grit mill and hopper,900
45 ft elevator to brick press hoppers (12 tons),100
6 Brick machines with hopper over and conveyor over,3,650
Iron roofing over plant,1,50015,000
Conversion of 10 open kilns to Schneiders,4,000
Erection of 6 new ones (Note 19) as shown,3,000
2 extra lifts for bricks and fuel,800
Hopper stages and gangways,7008,500
45,500

SUMMARY OF WORKING COST UNDER PROPOSAL "B".

sd
Cost per chalk ton f.o.b. South Ferriby 16d
freightage across 6d
discharge 2d
total 24d = per cement ton,210
Cost clay on wharf as at present (1902) say,14
Clay drying fuel,07
Motive power,05
Labor up to brick stage,09
Kiln labor,10
Kiln fuel,19
Kiln repairs,01.5
Repairs to dryers, conveyors, brick machines &c,06
Depreciation,03.4
Interest,03.4
Drawing kilns clinker to crushers say,05.7
TOTAL cost of clinker delivered at crusher,104

LIST OF PLANT DISPLACED BY PROPOSAL "B"
LIST OF CEMENT KILNS AND DRYING FLOORS (Note 20)

No.Typecapacity (Note 21)£ per tonValue £Future Value £remarks
1open (Note 22)60510510Can be converted to Schneider
2open609540480ditto; staging up from lifts
3Schneider802016001600(Note 23)
4open609540540staging up from lift; can be converted to Schneider
5open60510510 can be converted to Schneider
6open60510510ditto
7open607420420stands by itself; can be converted to Schneider
8open4062402408-10a in solid block; can be converted to Schneider
9open406240240can be converted to Schneider
10open306180180 no dome; can be converted to Schneider
10aopen306180180ditto (Note 24)
11Killick (Note 25)60127200Extra drying accommodation over pan capacity, the excess used to supply open kilns.
12Killick60127200
13Killick60127200
14Killick60127200
15Killick60127200
16Killick60127200
17Killick60127200
18Killick60127200
19Converted Batchelors27164320
20Converted Batchelors27164320
21Converted Batchelors27164320
22Converted Batchelors27164320
23Converted Batchelors27164320
24Converted Batchelors27164320
25Converted Batchelors27164320
26Converted Batchelors27164320
27Hilton27164320
28Hilton27164320
29Hilton27164320
30Hilton27164320
31Hilton27164320
32Hilton27164320
33Hilton27164320
34Hilton27164320
35Hilton27164320
36Hilton27164320
37Hilton27164320
38Hilton27164320
IBlock coke ovens000
IIBlock coke ovens000
19,8705,410
Neate's Wash mill, stones, harrows, mills, elevators, wheels & pumps700100at old machinery value
O&G ditto700100ditto
Mixing tanks & pumps500100ditto
Slurry pipes all over works600200ditto
Ropeway from Hiltons to Schneiders50040ditto
22,8705,950
Less present value5,950
Value to be written off & charged to cost of Proposal "B"16,920

CLINKER IS COSTING NOW ( 1902 ) NOT LESS THAN:-

Chalk.9/-
Clay (as in "B" also).1/4
Wet mill labour.-/10
Wet mill repairs.-/3
Kiln and floor labour.2/7
Kiln and drying house fuel.6/10.35
Faggots.-/0.75
Kiln repairs.-/10.9
Total21/10

This is 11s 6d more than under Proposal "B", and which saves £920 weekly equal to £47,840 per annum exclusive of 5% interest already charged, or, £2525 extra with it, making £50,365 total, being

OVER 110 PER CENT ON OUTLAY

From this gigantic saving the value of the plant displaced (£16,920) can be written off the first year.

Extra to it there will be about 5 or 6 acres of factory area not required and which if sold or let could provide cash for a great part of the outlay required for the work.

PROPOSAL C.

We will now consider this suggestion in detail. The outline of the scheme is:—

The chalk is brought to the storage hopper (and clay brought as now) and both washed as far of the slurry proving tank stage as in Proposal 'A", and then fed as liquid slurry into Rotary kilns.

The cost of slurry per cement ton under scheme "A" is,-

Chalk2/10
Clay1/4
Washing labour, fuel & repairs-/9
Total4/11

and to this now has to be added that for the rotary kiln to burn it.

Seven of them will, properly worked give an output of 1600 tons weekly (Note 26). At present they are far from perfect, but with intelligent management there is no doubt great improvements can be affected (sic) and yield far beyond 240 tons per week of 5½ days night and day (Note 27).

The labour may be safely taken as follows:-

  • 1 man stoking and driving engine for turning kilns & grinding coal.
  • 4 men Grinding the coal.
  • 4 men Burner and mate (two to work two kilns each).
  • 2 men Burner and mate to work the odd kiln.
  • 1 man as ganger to the lot.
  • 12 men per shift or 24 required for night and day work at 45/- each all round = £54 weekly and which equals 8¼d per ton for burning labour.

REPAIRS. If each kiln had £4 a week spent on it and which over a whole year would be more than enough to provide an entirely new lining for it (Note 28), this would be say £1500 for the lot, and add £500, a most liberal amount, for repair to any of the coal grinding gear and £250 more for engine or boiler providing turning power for it. Total £250, this equals 6½d per clinker ton.

KILN FUEL. If as much as 40% (Note 29) for this be consumed for burning wet slurry and including that used for power and drying the coal, and coal costs 10/- delivered on site . This will equal 4/- per clinker ton.

MILL LABOR, FUEL AND REPAIRS. Costs you now all inclusive with your present clinker say 3/4 and if it takes 20% more to grind the rotary clinker this will increase the cost under this head to 8d per ton.

OUTLAY REQUIRED.

Ferriby plant12,000
Wilmington plant,3,500
Lighterage plant,10,000
7 Rotary kilns (Note 30),14,000
Elevator to mill hopper,200
Coal grinding plant,1,500
Shed to cover same,2,600
Motive power for all say,800
Total44,500

DEPRECIATION. If on the whole of the kiln plant and building 10% p.a. (Note 31) is charged this means £1900 per year and equals 5½d per clinker ton.

INTEREST. 5% on same sum means 2¾d per ton on cement.

SUMMARY OF COST OF CLINKER MADE BY ROTARY KILNS FROM SLURRY

Cost of slurry under A scheme ( all per clinker ton)
Chalk2/10
Clay1/4
Washing expenses-/94/11
Rotary kiln
Labor-/
Repairs/
Fuel4/-5/
Mill labour fuel and repairs &c: increase over present cost-/8
Depreciation on kiln &c plan-/
Interest on Kiln outlay-/1/
Total cost delivered at mills11/6

Above it is shown your present cost is 21/10 for producing clinker delivered at the mill, thus showing there would be an estimated economy of 10/4 per ton which on 1600 tons output equals £825 weekly.

equal to per year,42,900
Less interest on value of chalk stocks,250
Less interest on value of coke stock,250
Interest & profit earned by lighterage,750
Interest on Ferriby outlay,600
Interest on Wilmington outlay,950
The whole of the land say 9 acres containing the whole of the old kilns, coke heaps, ovens, and chalk heaps, available for letting at say £500 annum not credited to this at all.
45,700

PROPOSAL D.

This suggestion is the same as B where the dry powdered chalk and clay are ready for use, after which instead of feeding brick machines it goes to Rotary Kilns for calcination (Note 32).

The powdered chalk is required and stored in hopper as in the other schemes A, B & C.

The clay is unloaded at the lower jetty beneath the chalk berth and dried. In this case, it is proposed to use the waste gas from the rotary kilns to dry the clay in these driers instead of using special fuel if they are erected in the position near the Killick kilns so as to permit this to be done and by which the estimated 7d per ton for drying fuel under scheme B would be saved.

From the octagonal blending hopper the material to ensure further incorporation and to still finer grind it, it passes as in C through the largest size grit mill, from this it is conveyed direct to the small hoppers over the rotary kilns.

The Labour previous to the kiln stage may be taken as follows:—

2 men wheeling clay from heap on wharf & feeding driers @ rate of 8 tons per hour. 2 at night and 2 on day duty @ £2 weekly each,8
1 man attending drier fan from kiln gases night and day,4
1 man superintending regularity of feed to drier and from same to pulverizer,4
1 man night and day attending mixing weighers under chalk and clay silos and conveyor and elevator therefrom to octagon tower chambers and using and attending shoots to grit mill @ £2 each,4
1 man attending grit mill and feed therefrom,4
Total24

This is on a 1600 ton output equals 3¾d per ton.

LABOUR on Rotary plant same as in C, which see = 8¼d per ton.

REPAIRS also, 6½d per ton.

KILN FUEL. This for dry material should undoubtedly be less by 5%, as found elsewhere, and we will take it at 35% (Note 33) with coal at 10/- per ton and equals 3/6 per cement ton.

MILL LABOUR, FUEL AND REPAIRS. Grinding the rotary clinker will be perhaps 20% harder to grind over the present cost and raise this charge at that amount = say 8d per ton.

ESTIMATE OF OUTLAY UNDER D

Ferriby plant as in A, B or C,12,00012,000
Lighterage ditto,10,00010,000
WILMINGTON PLANT.
1 hanging discharge elevator with motor and balanced bracket,600
1 elevator therefrom to hopper,500
Chalk storage hopper say,1,900
Weighing machine and shoots,300
3 rotary driers and stage & fan & kiln connections,2,000
Inclined clay conveyor,150
1 conveyor and 25ft elevator,100
1 pulverizer and hopper over,600
75 (ft) elevator to clay hopper,100
1 clay storage hopper,200
1 weigher and shoots &c,200
82 ft, spiral to octagon hopper,150
Octagon hopper in cement and iron,1,800
Mixing and filling elevators,300
Conveyor to grit mill,100
grit mill and hopper,900
conveyor to rotaries,150011,400
7 Rotary kilns,14,000
Conveyor to mill hopper,200
Coal grinding plant,1,500
Shed to cover kilns &c,2,600
Motive power for kilns80019,100
Total52,500

DEPRECIATION. If 5% be charged on the unloading plant 11,400 @ 5% = £570 and 10% on kiln plant. 19,100 @ 10% = £1910 or £2480 altogether and which equals 7¼d per ton.

INTEREST. on the outlay of £52,500 @ 5% p.a. = £2625 and is equal to a charge of 7½d per ton.

THE SUMMARY OF WORKING COST UNDER "D" IS THEREFORE:-

Cost of chalk2/10
Cost of clay on wharf1/4
Clay drying and blending-/
Rotary kiln labor-/
ditto repairs-/
ditto fuel3/6
Increased milling cost-/8
Depreciation-/
Interest.-/
Total per cement ton delivered at mill.11//

Compared with present cost for same thing of 21/10 (see above). This is 10/8¾ saved per ton, equal to £44,200 per annum on a 1600 ton output weekly.

To this has to be added:

Less interest value on chalk stocks,250
Interest & profit on lighterage,750
Interest on Ferriby outlay,600
ditto on Wilmington outlay,2625

Making a total earned, of £48,425 by the scheme in one year.

SUMMARY OF COSTS & ECONOMY GAINED.

(all based on 1600 cement ton weekly output.)

PROPOSAL APROPOSAL BPROPOSAL CPROPOSAL D
Estimated cost £ of outlay including £10,000 outlay which is optional on lighterage plant25,50045,50044,50052,500
Economy gained £ per annum over present cost of working29,37547,84045,70048,425
% of gain on outlay incurred, engineers charge & chalk contract fine not included117%110%102%92%
Kilns of existing plant made obsolete & not required016,92019,87022,370
Acres of works not required25910

CONCLUSIONS (Note 34)

After having given these 4 schemes a fair amount of thought and sketched same out on the attached tracings and estimated outlay and working costs as near as possible and on the safe side, after allowing liberally for depreciation, even if the whole result in any case were divided by 4 to allow 75% further margin for safety, the return on the outlay in either case will be so prodigious that the most apathetic of proprietors, ought to be aroused and at once be up and doing.

As any alterations at Wilmington are so painfully tedious, dilatory, and costly, I cannot really recommend much being done there, as it is certainly at the present day not the site for a cement works and I would more strongly recommend a new works be erected entirely in Lincolnshire on the site of the quarry and only a depot be kept at Hull for local trade and rail purposes in addition to one at Goole and Grimsby &c.

If your management say they must have a works at Wilmington then I suggest proposal A for a start, you doing your own lighterage by preference.

By this scheme either of the other proposals such as C or D can be then introduced without any loss of efficiency of scheme A which forms part of all the other 3. D in the most up-to-date and next to that is C, although B seems to earn the most return for the outlay, and is more cumbersome to work as it takes more room. It would however be less nuisance perhaps to the neighbourhood from smoke.

I think that a private Co, under the name of "Cement Ltd"' or "Ferriby Chalk Co", Coronet or Silex, or whatever Co, as a blind to your connection to same, get them to erect the works and start them and you do all the sales under your own name for as much as you wish to sell under the "Pelican" brand and the run on cheaper stuff invoiced from other office as if a distinct thing. You can then cater for the high class also cheaper trades, like we did with Anchor and Hilton brands. The Wilmington mass of antiquated plant can then be shut up any time and transferred to the new and main works.

There is no doubt; you can get the money and E.B. and many others would only be too glad to join you. Maxted could go on the Board as a blind to your own name which need not appear on the directorate.

I have prepared an outline sketch for a 2000 ton Works for Ferriby and am also preparing an approximate estimate of cost to erect it and the cost of manufacture and probable revenue, which I will send to you shortly.

The "Pelican" is a bird renowned for being sleepy and I am quite prepared after holding this report up to its eye to still see it remain standing on one leg and after shaking itself up a bit, relapse into an apathetic somnolent state, until some great eruption comes along in the shape of another works, thus robbing it of its regular amount of grub.

Then it will perhaps bestir itself, if it is not too late. However this further warning can only be thrown at it once more although the thrower is getting a bit tired of the throwing as his stones are getting a bit used up.

This stone is a bit harder than usual and he hopes it will hurt. If this allegorical cap fits, jam it well down over your ears.

Yours faithfully,

H. W. Anderson (Note 35)

Anderson recommended abandonment of the Wilmington site, and building a plant on the south bank. The Barton plant already existed, and was later provided with a rotary kiln, but was shut down in 1927. Subsequently, the South Ferriby plant was built further east. A major objection to new plants on the south bank was the lack of a rail link. To a southerner used to sending out most cement in nineteenth century sailing barges, this was not an issue - a wharf on the Humber was all that was needed. In fact, Earle was already investigating a chalk source directly opposite on the north bank, at Hessle, and when "local chalk" was finally adopted, this was the source, delivering crushed (but not ground) chalk by rail to Wilmington.

Anderson's suggestion of a "ghost" company to launch the new plant probably indicates fairly accurately the circumstances of the launch of Humber, and perhaps even Kirton Lindsey. The 2400 t/week Humber plant, delayed by the war, was built 1920-24, with George Maxted representing Earle's interests, as suggested. Having been "independently" built, the plant was absorbed into the Earle's organisation.

- o - O - o -

NOTES

Note 1. The six largest were Swanscombe, Bevans and Wouldham on the Thames, and Martin Earles, Burham and Peters on the Medway.

Note 2. Not given here.

Note 3. All schemes involved dry-grinding the chalk at the quarry site. The Kent chalk had been ground by washmill. The Humberside chalk is too hard to be treated by wash-milling, the effect of which is so gentle that hardly any grinding effect is achieved. The Barton plant ground the chalk to below 500 μm using edge-runners. For Wilmington, the powder would be barged across the river and unloaded to a storage hopper on the old chalk quay.

Note 4. All schemes retained the existing delivery of alluvial clay obtained from the south bank of the Humber and brought across by barge.

Note 5. Evidently Anderson had been at the Grand Opening of Edison's plant at New Village, Warren County, NJ (40.7189,-75.0647 on Google Maps), which took place in 1902. The plant had ten 80 ft dry process rotary kilns, making 2 t/hr each. Significantly, the plant shipped its first cement in 1905.

Note 6. This insane philosophy is still encountered today at plants where chemists had insufficient input at the design stage.

Note 7. It's obvious from the liberal use of the subjunctive that this blending system is something Anderson has designed on the back of an envelope. Ill-conceived blending systems gave the dry process a bad reputation before WWI. Those systems that achieved some degree of success were applied to "forgiving" raw materials close to kiln feed chemistry, such as marls, Blue Lias and slag. With the fairly pure raw materials as used at Wilmington, control from such a system would have been appalling.

Note 8. This sounds like an airline safety announcement - "if the cabin pressure ever changes . . ."! If fact, "poking down" would have been a permanent, frenzied activity.

Note 9. Schneider kilns needed feed in brick form, and this involved substantial extra plant and labour. If the bricks produced were house-brick sized, each would contain 4.47 kg of dry raw material. For the proposed plant output, 2520 tonnes of dry raw material were required per week, so 564,000 bricks were needed. Six machines running 130 hours a week would each need to make bricks at the rate of one every five seconds.This was expensive equipment and no spare capacity is allowed.

Note 10. Anderson could only use the information supplied by the plant, and the clay moisture was obviously the result of hyperbole. In manuscript, the 45% is deleted and replaced with 30%.

Note 11. The 1030 is also deleted in manuscript and replaced with 720. This means that the 566 tons of dry clay in the original is replaced with 504 tons in the modified data - showing that even the clay content of the rawmix is not known with any precision. It's hard to be quantitative in these circumstances.

Note 12. Use of 0.2 kg coal to evaporate 1 kg of water as a rule-of-thumb is somewhat excessive. Modelling a rotary drier swept with two-fold excess combustion air, an exit temperature of 120°, and 10% shell losses, heat requirement is 3776 kJ per kg water evaporated, whereas 0.2 kg steam coal would yield 6200 kJ.

Note 13. Another rule-of-thumb: 4 lb/hr of coal is required to generate 1 HP of motive power. In SI units, this is 6.759×10-4 kg/s per kW. If the coal has 31,000 kJ/kg, then this is 20.95 kW of fuel heat per kW of motive power, or 4.77% efficiency. Evidently this was considered normal at the time.

Note 14. The job sounds bad enough as it is - standing up making one brick every five seconds for a twelve hour shift. Getting paid 0.0128 old pence per brick as a productivity incentive would not have done much to improve it.

Note 15. Reviewing the wages paid, there are four distinct wage rates: £1 a week for "lads", £1.5 for burner's mates, £2.5 for brick makers, and £2 for everyone else, including kiln burners. On Thamesside at least, kiln burners were already paid considerably more than others. The use of 17 Schneider kilns indicates that these were expected to make 96 t/week each. 80 t/week was typical.

Note 16. Water quenching was sometimes used to speed up the turnaround of bottle and chamber kilns.

Note 17. With coke of 30 MJ/kg, this would be a kiln heat consumption of 5.25 MJ/kg clinker, which was fairly typical.

Note 18. Anderson left this blank. If the clay used was the 1030 tons mentioned earlier, the cost per clay ton was 2/1: if it was 720 tons, then it was 3/-.

Note 19. Schneider kilns cost only £500 each, and if all 17 had been constructed new, this still would have been only 34% of the Wilmington site project cost.

Note 20. This list gives a useful snapshot of the plant at the turn of the century. A contemporary letterhead gives a somewhat idealised view of the plant at this time:

Wilmington 1924

A. - 8 Batchelor kilns
B. - 12 Hilton kilns
C. - Main power plant
D. - Roman kiln bank
E. - Finish mills - remained located here until 1969
F. - Chalk wharf and main washmills
G. - 6 large bottle kilns
H. - Stores, maintenance etc.
I. - 8 Killick kilns
J. - Clay wharf and washmills
K. - Main cement store and packing area
L. - Offices
M. - Original Roman cement plant site

Note 21. The sum of the capacity numbers is 1600 tons/week - the value used in Anderson's designs. This implies a yearly output of 84,800 tonnes. In fact, the best year's output (and that exceptional) was only 87% of this. The capacity of the bottle kilns indicates that they were "forced" and perhaps run semi-continuously. Elsewhere it is mentioned that the clinker was water-cooled.

Note 22. "Open kiln" was the standard misnomer for any kiln with a lime-kiln-style hearth, other than chamber kilns, which were "closed". All the "open" kilns (except 10/10a) were tall bottle kilns, as seen in the picture above.

Note 23. One bottle kiln had been converted to a Schneider in around 1900 as an experiment. It was regarded as a failure, and this probably doomed the cheap-and-cheerful option B.

Note 24. Kilns 10 and 10a were literally "open", having no bottle extension, and were used for Roman Cement. By this time, Roman cement production was limited to two or three 15 tonne burns per year.

Note 25. Killick kilns were "double" kilns along similar lines to Gibbons kilns.

Note 26. To make 1600 t/week with seven kilns running continuously, they need to make 33 t/d. No British rotary kiln was achieving this at the time, but larger kilns were being installed at Bevans and Martin Earles, so maybe larger kilns were being suggested, as Anderson had seen at the Edison plant.

Note 27. Does he really think that rotary kilns run 5½ days a week?

Note 28. This sounds extremely optimistic, since frequent refractory failure was a common feature of all the early rotary kilns.

Note 29. Most kilns did better than this. If the coal is the same 31 MJ/kg steam coal as used elsewhere - the price is the same - then this would be a kiln energy consumption of 12.4 MJ/kg. Most early wet kilns were below 11 MJ/kg.

Note 30. £2000 per kiln. If the installation makes 80,000 tonnes a year, then this is £0.175 per annual tonne, or £17.5 in 2016 money. The other plant site items raise this by 36%.

Note 31. This implies a life expectancy of ten years. With hindsight, none of the early kilns lasted that long.

Note 32. At this stage, no dry process rotary kilns had been installed in Britain. The four systems installed before 1910 (Norman, Kirtlington, Southam and Premier) all used argillaceous limestones, producing rawmixes that could function without intensive blending. So also did the Edison plant that Anderson had seen. In the Wilmington case, a dry process installed with the speculative blending system suggested would have been doomed to failure.

Note 33. Norman ran at about this level - subsequent kilns were better.

Note 34. Here Anderson gives an object lesson in "how to be a consultant". One suspects that, while he was preparing the report, Anderson's conversations with Earle led him to conclude that his recommendations would be ignored.

Note 35. On the last page, Earle added in manuscript a suitably shirty response to this.

Note 36.

Note 37.

Note 38.

Note 39.

Original content © Dylan Moore 2011: commenced 07/08/2011: last edit 14/07/2017.

Return to plant list

HOME