Tímarit Verkfræðingafélags Íslands - 01.12.1967, Page 102

Tímarit Verkfræðingafélags Íslands - 01.12.1967, Page 102
100 TÍMARIT VFl 1967 places that heat can be produced that cheap with conventional fuels. Freeze-dried products have many advantages, such as the fact, that the weight of the finished products — for instance fish — is only about 20% of the raw-product. No refrigeration or similar costly methods are required for keeping the product. In this respect freeze-dried pro- ducts are comparable to the fish-protein con- centrate which will be discussed later in this conference. On the other hand, freeze-dried fish can be reconstituted, as such, at the consumer end. In this connection I hope I will be excused if I quote Dr. Pariser’s paper, which has not yet been read. Dr. Pariser quotes the processing cost for fish protein concentrate as about 14 cents per pound of the finished product. This includes the price of fish at 1 cent per pound, and that corresponds to about 6,7 cents per pound in the price of the finished products, if the yield is 15% as quoted. As a comparison, I mention from Dr. Petersen’s paper that the total processing cost in freeze-drying is 7V2-15 cents per kg of water evaporated. This corres- ponds in the case of fish to approximately 13-26 cents per pound of freeze-dried product. If we add to this 5 cents per pound for the raw-fish at the same priee, one cent per hour, we get about 18-31 cent per pound as a compar- able figure to the 14 cents per pound for the FPC, quoted by Dr. Pariser. In other words, according to those figures, the price difference is only of the order of 30-80%. This is not much of a difference when you keep in mind that in the case of the freeze-drying you can offer the consumer practically the natural product, whereas in the case of the FPC, you have a product that is vastly different from the original one, even if it is in all other respects a first class product. I am aware of the danger of making this comparasion, and it applies only to the orders of magnitude, the figures may not be found entirely on the same basis. But I would like to point out that due to the special circumstances here in Iceland, the low energy cost, and the fact that we have enormous potential of low- priced fish, the herring, which is not used per- haps in the best way as yet, I do suggest that it would be worth studying, whether those two resources could be connected together in a profitable way. Pétur Sigurjónsson: I would like to thank Mr. Begtrup-Hansen for this article. What we have seen here is the be- ginning of a new industry and we have had it pointed out that the development of the machinery is still going on very fast, and in two respects. Firstly to cope with the high costs of the final product as it is now, and also to find out new types of products. As we have heard here the main costs are the capital cost and the costs of energy. But I know there is an enormous lot of research done in this field, and the machinery we have seen here is — as we could say — a more universal apparatus where you could freeze-dry anything you want. But in the latest developments, you go on to more specialized machinery where you take account of the product you are going to use and then construct the machinery with that in view. It is about these latest developments in this field that I would like Mr. Begtrup-Hansen, to teil us. There is the new cylinder freeze-drying machinery, where you, for instance in the “Dutch Sheffingsystem”, fill in the cylinder and freeze a layer of the product on the inside of it through the evaporation of ammonia. When the layer of products is frozen you put on vacuum, and by reversing the process you heat up the cylinder by compressing the ammonia again — so you have a sort of a heat-pump. This process is claimed to be only half as expensive as the conventional freeze-drying as we have seen it here to-day. The United States Department of Agriculture is also developing a cylinder freeze-drying process where you transfer the heat to the goods — granulated goods — with rotating fins. You get a very intensive heat-transfer and very short drying time, even down to 3 hours, so the processing cycles are very short and the capital- costs are lower. Then there is also new Spray freeze-drying. As you have seen here to-day they are going away from contact-heating over to radiant- heating, and there are developments in short- wave-heating also to make the process still more economical and intensive. These are the questions I would like to have cleared.
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