I thought some of you would get a laugh out of this. The text found and forwarded to me by my wife Vandy. Remember those descriptions of pieces I had done for the long lost 'Outlander' film? Well everyone jumped on the bandwagon of our Anglo-Saxon Hero a while back. The lastest version is just hitting the theatres - and the * trailer * even looks like a bad video game...
From Antagony and Ecstasy, one of the movie review sites Vandy reads:
A cartoon is coming, || computer-created,
Generated on green-screen , || the graphics laid over.
Beowulf is the book || bound for the movies,
Retold by that rascal || Robert Zemeckis,
His camera is clumsy || compulsively gaudy.
The trailer is terrifying || a tragic misfire
Of video unviewable || and a valley uncanny,
The proud performers || plastic and ugly
Tuesday, November 13, 2007
Wednesday, November 07, 2007
Riverdale House - 2nd Install
On Tuesday (Nov 6) I installed the next two units of the Riverdale House railing project in Toronto

The third piece of the project was a half circle railing, 48 inches in diameter. To make both my fabrication, but more importantly transportation, easier, this was made in two pieces. A central leg was required to support the centre of the panel, so it proved fairly simple to run three bolts to joint the sections. This approach also allowed for a slight bit of flex to the curve during installation. Despite my butter fingers (after a three hour drive into Toronto) this unit fit its space exactly and proved quite quick and easy to secure into place. On subtle feature of this panel was that the leg piece had been hot punched with the names of the client and the date.

The fourth piece installed was the right hand (seen from the street) stair hand rail. This is the straight section. This proved a wee bit more of a problem to fit. Of course none of the angles on the wooden stairs proved to be at 90 degrees to each other - which can prove a series problem on a 9 foot long diagonal. In the end the railing fit fairly well. I had come prepared with some wooden shims (just in case). By lifting the lower support at the top deck level about a half inch, the rest of the support pieces fit pretty close. It proved possible to screw down the various attachment points tight to the existing stairs. I was quite pleased with how solid the finished hand rail was when fully attached with the lag screws.

This is a final view of the elements installed so far as they appear from the sidewalk. One panel remains - the curved hand rail for the left side stairs.
Further details can be seen on the main Wareham Forge web site :
www.warehamforge.ca/work-in-progress
The third piece of the project was a half circle railing, 48 inches in diameter. To make both my fabrication, but more importantly transportation, easier, this was made in two pieces. A central leg was required to support the centre of the panel, so it proved fairly simple to run three bolts to joint the sections. This approach also allowed for a slight bit of flex to the curve during installation. Despite my butter fingers (after a three hour drive into Toronto) this unit fit its space exactly and proved quite quick and easy to secure into place. On subtle feature of this panel was that the leg piece had been hot punched with the names of the client and the date.
The fourth piece installed was the right hand (seen from the street) stair hand rail. This is the straight section. This proved a wee bit more of a problem to fit. Of course none of the angles on the wooden stairs proved to be at 90 degrees to each other - which can prove a series problem on a 9 foot long diagonal. In the end the railing fit fairly well. I had come prepared with some wooden shims (just in case). By lifting the lower support at the top deck level about a half inch, the rest of the support pieces fit pretty close. It proved possible to screw down the various attachment points tight to the existing stairs. I was quite pleased with how solid the finished hand rail was when fully attached with the lag screws.
This is a final view of the elements installed so far as they appear from the sidewalk. One panel remains - the curved hand rail for the left side stairs.
Further details can be seen on the main Wareham Forge web site :
www.warehamforge.ca/work-in-progress
Labels:
blacksmith,
contemporary arts
Thursday, November 01, 2007
Icelandic Smelt Two (report)
Stone Slab with Low Air
As was mentioned earlier, the DARC fall smelt was originally intended to follow on the development of an Icelandic style smelter.
Chamber size at Tuyere : 25 cm (front to back) x 35 cm (side to side)
Total furnace Height : 70 cm (random)
Shaft Height above Tuyere : 40 cm (minimum)
Height of Tuyere above base : 18 cm
Tuyere angle : starts at 26 down, latter shifted to 10 down
Tuyere size : standard 2.6 cm ID steel pipe
It was expected that the lower air volumes would greatly extend the time required for the smelt. Although better intentions were made, the pre-heat was started at our normal 9 AM, with primary smelt sequence started a bit after 10 AM. As normal, pre-heat was using wood splints, passive at the start and for the last 15 minutes or so using gentle air.
For this smelt, Neil was the iron master, with Ken working as lead hand. Darrell started the recording, with Ron Ross managing the latter half of this task.
It was decided to seed the smelt using the poorer quality Virginia Rock ore gathered last year by Darrel and Vandy. Although this material has proved to have too low an iron content, it was hoped that it would compensate for the lack of slag seen with earlier uses of the hematite grit. It was also expected that considerably less slag would be available inside this smelt with the use of stone instead of clay for the wall materials. In the end it proved we were overly conservative, and production of a suitable volume of slag would prove a problem.
With the lower consumption rates expected as a result of the lower air volume, it was also decided to limit the total amount of ore added. It was expected that this would only allow for the formation of a small bloom. The air volume used over this smelt was about 400 litres per minute - compared to the usual rate employed in past successful smelts at closer to 800 plus LPM. As was expected, the lower air greatly extended the time between additions of the standard 10 litre charcoal measure, which increased from a normal 8 minute average to closer to 22 minutes. The construction of the furnace had reduced the height of the reaction column from our normal 55 - 60 cm to closer to 40 cm. Still the theoretical 'drop time' for any individual particle of ore had been extended from a normal 25 - 30 minutes to double that - closer to 60 - 70 minutes. This was expected to produce problems in carbon control with the fine particles of the hematite grit.
Over the course of the smelt, the following totals were recorded:
Ore : 12.3 KG (10 kg hematite grit / 2.3 Virginia rock)
Charcoal : 170 litres + 6 kg ungraded fuel at start
Time : Main sequence = 6 hours
Generally the slower consumption rate lead to a much less frantic smelt sequence. It was obvious fairly early on that less slag was being produced. Although the furnace had been constructed as an 'incontinent' type, little slag was ever observed flowing from the slag bowl (even after the tap arch was opened latter in the smelt).
The next day the cold smelter was excavated, with a good photographic record made and representative samples collected. All the slag was collected, and the area was cleaned with the large magnet. The results of this work:
Weight of Slag : 3.5 KG
Weight of Reduced Ore (but poorly or not sintered) : 3 KG
Weight of 'Bloom' (fragments) : 2 KG
Conclusions:
1) The construction method using stone slabs with clay cobb sealing the joints is certainly viable. It is unlikely that the mica schist material would withstand a second firing without heavy replacement of the material at the normal hot zone above the tuyere. The stone in this area exhibits both considerable erosion and also a thick deposit of slag. Both of these effects should remain clearly visible in archaeological remains of this type.
2) The use of lower volume air requires considerable further experimentation to develop a truly successful sequence. As has been clearly demonstrated with both our earlier smelts and those of other experimenters - there is a (poorly understood) relationship between ore type and purity, smelter material and design, fuel preparation, and physical sequence. Those attempting smelts with low air volumes have great difficulty (if able at all) in producing large and well consolidated blooms.
3) In retrospect, it is most likely that both the content and the fine particle size of the hematite grit renders it quite unsuitable for use in any kind of low slag producing smelter. The extremely low silica content of the ore means that the formation of slag must come almost exclusively from the melting of the smelter walls. Although good results have been attained with this material in past smelts, this has always been inside those furnaces that have suffered considerable internal erosion.
As was mentioned earlier, the DARC fall smelt was originally intended to follow on the development of an Icelandic style smelter.
Chamber size at Tuyere : 25 cm (front to back) x 35 cm (side to side)
Total furnace Height : 70 cm (random)
Shaft Height above Tuyere : 40 cm (minimum)
Height of Tuyere above base : 18 cm
Tuyere angle : starts at 26 down, latter shifted to 10 down
Tuyere size : standard 2.6 cm ID steel pipe
It was expected that the lower air volumes would greatly extend the time required for the smelt. Although better intentions were made, the pre-heat was started at our normal 9 AM, with primary smelt sequence started a bit after 10 AM. As normal, pre-heat was using wood splints, passive at the start and for the last 15 minutes or so using gentle air.
For this smelt, Neil was the iron master, with Ken working as lead hand. Darrell started the recording, with Ron Ross managing the latter half of this task.
It was decided to seed the smelt using the poorer quality Virginia Rock ore gathered last year by Darrel and Vandy. Although this material has proved to have too low an iron content, it was hoped that it would compensate for the lack of slag seen with earlier uses of the hematite grit. It was also expected that considerably less slag would be available inside this smelt with the use of stone instead of clay for the wall materials. In the end it proved we were overly conservative, and production of a suitable volume of slag would prove a problem.
With the lower consumption rates expected as a result of the lower air volume, it was also decided to limit the total amount of ore added. It was expected that this would only allow for the formation of a small bloom. The air volume used over this smelt was about 400 litres per minute - compared to the usual rate employed in past successful smelts at closer to 800 plus LPM. As was expected, the lower air greatly extended the time between additions of the standard 10 litre charcoal measure, which increased from a normal 8 minute average to closer to 22 minutes. The construction of the furnace had reduced the height of the reaction column from our normal 55 - 60 cm to closer to 40 cm. Still the theoretical 'drop time' for any individual particle of ore had been extended from a normal 25 - 30 minutes to double that - closer to 60 - 70 minutes. This was expected to produce problems in carbon control with the fine particles of the hematite grit.
Over the course of the smelt, the following totals were recorded:
Ore : 12.3 KG (10 kg hematite grit / 2.3 Virginia rock)
Charcoal : 170 litres + 6 kg ungraded fuel at start
Time : Main sequence = 6 hours
Generally the slower consumption rate lead to a much less frantic smelt sequence. It was obvious fairly early on that less slag was being produced. Although the furnace had been constructed as an 'incontinent' type, little slag was ever observed flowing from the slag bowl (even after the tap arch was opened latter in the smelt).
The next day the cold smelter was excavated, with a good photographic record made and representative samples collected. All the slag was collected, and the area was cleaned with the large magnet. The results of this work:
Weight of Slag : 3.5 KG
Weight of Reduced Ore (but poorly or not sintered) : 3 KG
Weight of 'Bloom' (fragments) : 2 KG
Conclusions:
1) The construction method using stone slabs with clay cobb sealing the joints is certainly viable. It is unlikely that the mica schist material would withstand a second firing without heavy replacement of the material at the normal hot zone above the tuyere. The stone in this area exhibits both considerable erosion and also a thick deposit of slag. Both of these effects should remain clearly visible in archaeological remains of this type.
2) The use of lower volume air requires considerable further experimentation to develop a truly successful sequence. As has been clearly demonstrated with both our earlier smelts and those of other experimenters - there is a (poorly understood) relationship between ore type and purity, smelter material and design, fuel preparation, and physical sequence. Those attempting smelts with low air volumes have great difficulty (if able at all) in producing large and well consolidated blooms.
3) In retrospect, it is most likely that both the content and the fine particle size of the hematite grit renders it quite unsuitable for use in any kind of low slag producing smelter. The extremely low silica content of the ore means that the formation of slag must come almost exclusively from the melting of the smelter walls. Although good results have been attained with this material in past smelts, this has always been inside those furnaces that have suffered considerable internal erosion.
Labels:
iron smelting,
Viking Age
Recording Smelting Slags
In the recent set of conversations backgrounding the Icelandic smelter series, Kevin Smith had asked me if we had been keeping any records of the amount of slag produced in each experiment. Truth is that although we have numbers for ore and bloom, we generally have no records for the amount of actual slag created. This is certainly a significant measurement, as there are very few metal blooms found - these were just too valuable considering the effort that had gone into creating them. Slag, on the other hand, is nothing more than a waste product, and an extremely durable one at that. There are literally tons of various slags, even within a single major historic iron producing site. Hals in Iceland, for example, Smith estimates there is some 5000 kg of waste slag. *
Slag remains are also used by modern researchers to estimate the probable yields of individual ancient smelts:
- First the ore utilized will be examined. Normally it is expected that there will be some 'slop' of ore to be found right close to the shaft of the furnace. (In our own work, we always end up dropping some ore material by accident as it is added to the top of the furnace.) By analyzing the relative iron content of that ore, an idea of the starting ratio of iron and other waste products (which will go to the slag) can be gathered. As has been pointed out by other contributers to the Early Iron discussion, there can be a couple of reasons why the ore materials found around a smelting area could be misleading. Ideally an experienced worker can make a good judgment of the suitability of an individual piece of ore at the gathering location. In many cases however, our own experience has shown that it is only after ore is roasted and broken for size that good quality may become apparent. Much of the ore found around a smelter site may actually represent this discarded material. Little (if any) of the actual ore utilized for the smelt itself may remain.
- Next the slag itself is analyzed for the remaining iron content. This can only supply the roughest of estimates for a number of reasons. The slag found will certainly vary considerably. The quality of the slag will change over the course of a smelt, from the viscous bubbly iron poor slag at the first stages, eventually becoming a thin hard iron rich material in the latter stages. Slag from any given point in the several hour process of the smelt can be quite different in composition. Even inside a large slag block from a single smelt event, there is certainly differences in iron content remaining at various points within the mass.
- Not only the ratio of iron and silica from the ore effect both volume and nature of the slag, but the materials and set up of the furnace itself have a major effect. Different wall materials will erode at quite different rates, and of course melted furnace walls are a major component of slag. Generally only the very base levels of a furnace will remain to be examined. so at best the amount of
- The mechanics of a single smelt will greatly effect the way slag may be scattered over a working area. In most cases these processes will change the visual appearance of the slag materials. Tap slag will have distinctive flow patterns for example. As hot slag is always a problem to the operators, discarded slags may be tossed some distance away from the working area. Our own experience has shown that a large amount of material may be pulled away from the slag bowl inside the smelter when the bloom is extracted, especially if a bottom extraction method is used. This material usually has a certain amount of partially sintered ore with it. (What Sauder & Williams call 'mother'.) This loose material is going to be found not at the smelter, but at the area where the initial consolidation of the hot bloom is to be carried out. This location is certain to be close by to the smelter, but may in fact be removed by a number of metres (and thus may not be uncovered by the excavation at all)
In our own experiments, we have generally been working with ores that run in the range of 60 - 70 % iron content. Our yields vary considerably, but run from about 30 - 40 % metallic bloom against ore.
For the last two smelts, we have attempted to recover as much of the slag produced as possible. This can hardly be considered a representative sample, more (and more detailed) observations need to be made.
Note : On Icelandic TWO, the 5 kg listed includes all materials recovered
- 1.7 kg small un-sintered fragments
- 2.3 kg badly sintered pieces (larger than 6 mm)
- 1 kg roughly golf ball sized denser pieces (considered true bloom)
Overall the material produced from this smelt proved too fragmented to forge, with an extremely high carbon content.
* With my recent focus on Hals in Iceland, I would be remiss if I did not provide readers with the reference for further details:
'Ore, Fire, Hammer, Sickle: Iron Production in Viking Age and Early Medieval Iceland'
Kevin Smith
Kevin has become a good friend and a close advisor to our experimental work over the years. He has contributed considerable depth to my understanding of the archaeology of iron smelting through our ongoing personal communications.
Slag remains are also used by modern researchers to estimate the probable yields of individual ancient smelts:
- First the ore utilized will be examined. Normally it is expected that there will be some 'slop' of ore to be found right close to the shaft of the furnace. (In our own work, we always end up dropping some ore material by accident as it is added to the top of the furnace.) By analyzing the relative iron content of that ore, an idea of the starting ratio of iron and other waste products (which will go to the slag) can be gathered. As has been pointed out by other contributers to the Early Iron discussion, there can be a couple of reasons why the ore materials found around a smelting area could be misleading. Ideally an experienced worker can make a good judgment of the suitability of an individual piece of ore at the gathering location. In many cases however, our own experience has shown that it is only after ore is roasted and broken for size that good quality may become apparent. Much of the ore found around a smelter site may actually represent this discarded material. Little (if any) of the actual ore utilized for the smelt itself may remain.
- Next the slag itself is analyzed for the remaining iron content. This can only supply the roughest of estimates for a number of reasons. The slag found will certainly vary considerably. The quality of the slag will change over the course of a smelt, from the viscous bubbly iron poor slag at the first stages, eventually becoming a thin hard iron rich material in the latter stages. Slag from any given point in the several hour process of the smelt can be quite different in composition. Even inside a large slag block from a single smelt event, there is certainly differences in iron content remaining at various points within the mass.
- Not only the ratio of iron and silica from the ore effect both volume and nature of the slag, but the materials and set up of the furnace itself have a major effect. Different wall materials will erode at quite different rates, and of course melted furnace walls are a major component of slag. Generally only the very base levels of a furnace will remain to be examined. so at best the amount of
- The mechanics of a single smelt will greatly effect the way slag may be scattered over a working area. In most cases these processes will change the visual appearance of the slag materials. Tap slag will have distinctive flow patterns for example. As hot slag is always a problem to the operators, discarded slags may be tossed some distance away from the working area. Our own experience has shown that a large amount of material may be pulled away from the slag bowl inside the smelter when the bloom is extracted, especially if a bottom extraction method is used. This material usually has a certain amount of partially sintered ore with it. (What Sauder & Williams call 'mother'.) This loose material is going to be found not at the smelter, but at the area where the initial consolidation of the hot bloom is to be carried out. This location is certain to be close by to the smelter, but may in fact be removed by a number of metres (and thus may not be uncovered by the excavation at all)
In our own experiments, we have generally been working with ores that run in the range of 60 - 70 % iron content. Our yields vary considerably, but run from about 30 - 40 % metallic bloom against ore.
For the last two smelts, we have attempted to recover as much of the slag produced as possible. This can hardly be considered a representative sample, more (and more detailed) observations need to be made.
| EVENT | Icelandic ONE | Icelandic TWO | ||
| DATE | 10/8/07 | 10/27/07 | ||
| SMELTER | Norse short shaft | Norse short shaft | ||
| CONSTRUCTION | clay slab / stone plate | stone slab | ||
| NOTE | start low, high majority | low air volumes | ||
| ORE TYPE | hematite | hematite | ||
| WEIGHT | 12.3 | 12.3 | ||
| BLOOM | 6 | 5 (see note) | ||
| TYPE | dense lens | badly sintered | ||
| SLAG | 8.5 | 3.5 | ||
| TYPE | complete bowl | broken pieces | ||
| TAPPING | none | incontinent | ||
| OTHER | no mother measured | all included |
Note : On Icelandic TWO, the 5 kg listed includes all materials recovered
- 1.7 kg small un-sintered fragments
- 2.3 kg badly sintered pieces (larger than 6 mm)
- 1 kg roughly golf ball sized denser pieces (considered true bloom)
Overall the material produced from this smelt proved too fragmented to forge, with an extremely high carbon content.
* With my recent focus on Hals in Iceland, I would be remiss if I did not provide readers with the reference for further details:
'Ore, Fire, Hammer, Sickle: Iron Production in Viking Age and Early Medieval Iceland'
Kevin Smith
Kevin has become a good friend and a close advisor to our experimental work over the years. He has contributed considerable depth to my understanding of the archaeology of iron smelting through our ongoing personal communications.
Labels:
iron smelting
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