A METHOD OF DRYING DAMP ORGANIC MATERIAL

Abstract: Apparatus for drying damp material, such as pro­ teinaceous material, comprises a heat source and a rotating chamber. This chamber is formed from an inlet chamber (6) and a second chamber (10). The temperature in the inlet chamber is high, whereas the temperature in the second chamber is lower and the material to be dried is held in the hot inlet chamber for a shorter period of time than the cooler second chamber in which it is held before the dried product is recovered from an outlet end (12).

Description: This invention relates to a method of drying damp material to obtain a product with a predetermined moisture content. From a meat rendering plant three products are produced, tallow, meal and waste water. The meal will comprise a high proportion of protein and bone, if bone is processed at the same time. This meal has a market as an animal feed the price of which depends on the degree of available protein in the meal. When drying the meal after removal of the tallow and the majority of the waste water, there are two or optionally three requirements, the first is to remove as much water as is required, generally to less than 8%, the second is to avoid denaturing the protein, and the third option is to sterilise the meal when it is necessary. Balancing all three factors together has resulted in drying by indirectly heating through jacketed steam vessels. Temperatures in the vessel in the range of 110-135 o C are the normal temperatures employed with residence times of 2-3 hours being used. At these temperatures there is still some denaturing of the protein because of the long residence time. By drying at such temperatures it is not possible to remove wool or other hair residues. Such may be present in small amounts but such small amounts can lead to a much lower grading for the product and hence a lower price. Sterilisation can be achieved by other means than in the drying step. Rotary driers have been used heated by combustion of a suitable fuel. Because of fires which have commonly developed such driers have not proven to be commercially successful for drying organic materials. The reason for such fires is considered by the current applicant to be that the rate of flow of the material passing through the naked flame was not adequately controlled. There are other materials where a product needs to be dried to a predetermined moisture content. A number of standards for various materials require drying to achieve a moisture content of 8% or less. At this level of moisture most products are stable for long term storage. The problems of drying to a predetermined moisture level are the difficulty in establishing precisely when that moisture level has been reached. Thus overdrying is normally undertaken to ensure compliance with the standard. This results in increased fuel cost and increased damage to the product. Other products where moisture content may vary are blood from meat processing works, grain, sewage sludge and the like. The majority of these materials are of organic origin and it is drying of these materials which is the main purpose of the current invention. It is however envisaged that the process and the apparatus of the invention can be used to dry other materials. US-A-2715283 discloses a method of drying damp organic material wherein surface moisture is flashed off in a first zone and the material is dried in a second zone at lower temperature. According to US-A-4177575 the material is supplied to the dryer such that it falls onto the inner surface of an inclined, cylindrical drying zone. This invention provides a process in which the damp feedstock is subject to controlled temperature drying consisting of a first very hot zone and then through a zone of decreasing temperature according to the features of claim 1. In the method of the invention the initial high temperature zone is designed to be as hot as possible to flash evaporate surface moisture and also to flashburn any fine hair residues that may be present, but insufficiently high as to cause significant denaturing of the protein or damage to other organic material that may be present. The residence time in this zone is short, such time being dependent upon the particular temperatures employed to ensure the above criteria are met. The temperature needs to be at least about 750 o C but desirably less than 900 o C, with the residence time being a few seconds. The heating is desirably by direct heat transfer from a live flame for greatest energy conversion, the heat being transferred by natural convection and radiation desirably assisted such as by a compressed air blower driving air through the live flame of the burner to create the hot zone. It is important in accordance with this invention to minimise contact of the proteinaceous material with the live flame as control over the degree of denaturisation is difficult which can even lead to the feedstock starting to burn. Preferably there is no contact. The feedstock moves from the hot zone into a lower temperature zone which can be a continuation of the hot zone but more remote from the combusion chamber. In this zone, the temperature gradient can be relatively uniform from close to that of hot zone down to a temperature at the outlet end desirably above 100 o C. A temperature below 100 o is undesirable as it is difficult to sufficiently dry the product. The residence time in such chamber can vary from a few minutes up to an hour or even more. But for reasons of economy it is desired to keep the residence time as short as possible whilst still obtaining a dried product. In accordance with this invention it has been found that by the controls referred to above it is possible to use a rotary drying cylinder to dry the feedstock. The drier will have suitable means for feeding in the wet feedstock desirably in a continuous manner such as from the outlet of the meat processing plant. This invention is principally envisaged to be of use in drying damp bonemeal in a meat processing plant and will hereinafter be described with reference to that method. Because the characteristics of the product from the outlet of the meat processing plant as well as the flow rate thereof can vary considerably dependent on the nature of the material being processed and speed of operation, it is a preferred feature of this invention to continuously monitor the temperature of the drier and automatically adjust the heating means to ensure that the temperature of the hot zone and the outlet is at a satisfactory level. One method currently envisaged is to have a temperature sensor at the outlet designed to generate a signal whenever the temperature varies from 110 o by a desired temperature such as 5 o , more specifically 2 o . The generated signal is designed to automatically increase or decrease the output of the heating source to thus raise or lower the temperature within the drier. It is considered feasible by such adjustment techniques to ensure that the inlet zone temperature is above the desired minimum temprature which will generally be 750 o C. It is envisaged within the invention for a temperature sensor to be placed within the hot zone and which is designed to generate a signal to be read in conjunction with the signal from the sensor in the outlet. Such "hot zone" sensor can be designed to maintain the temperature within the hot zone in the range of 750 to 900 o C. The signals from the hot zone sensor and outlet sensor can be compared and variation to the output of the heating source and/or rotation speed of the dryer altered to achieve the desired outlet temperatures. The drier desirably agitates the feedstock e.g. by inwardly protruding baffles so that the feedstock is suspended within the cylinder for much of its length. This improves the drying speed. The temperature gradient can be achieved by making the drying system one continuous chamber with the hot zone at the front leading into the lower temperature zone. The temperature gradient can be achieved by forcing air through the flame in the combustion chamber and by suitable choice of the speed of the air and length of the various chambers, the desired temperature ranges can be achieved. In order that the residence time in the hotter zone at the front of the cylinder is short, this section of the rotating chamber has a floor sloping at a greater angle than the remainder of the chamber. In order to assist in forward movement of the feed forwardly directing baffles can be provided. It has been found that these baffles need not be greatly pronounced. For example a simple helical raised rib on a cylindrical chamber floor can be effective. It is a further preferred feature of the invention for exhaust gases to be recycled. In this way as much of the available energy units in the fuel can be utilised. It is desirable to dehumidify at least part of the exhaust gases to reduce the build up of moisture within the drying chamber. It is also desirable to cool the dehumidified gases preferably to 30 to 60oC to further increase the humidity uptake of this portion of the gases. By suitable choice of the proportion of the streams of recycled gases the maximum utilization of the heat values together with rapid continuous drying can be achieved. An apparatus for carrying out the invention is described by way of example with reference to the accompanying drawings in which Figure 1 is a plan schematic view of one form of drier for use in this invention, Figure 2 is the side elevation of the drier of Figure 1, Figure 3 is a cross section of the drier of Figure 1 and Figure 4 is a perspective view of the inlet of the drier. As shown in the drawings the drier is preferably a continuous tube having two sections, a combustion chamber 1 and a drying chamber consisting of two parts, a hot zone 6 and a cooler zone 10. The cold zone 10 is desirably cylindrical while the hot zone 6 is desirably of a truncated conical shape. Feed material such as wet proteinaceous material from a rendering plant is fed into hot zone 6 by screw conveyor 2. The feedstock can be continuously fed from the outlet of the rendering plant. Since the outside surface of the conveyor 2 is exposed to the hot zone it is a desirable feature of this invention to provide insulation means about the conveyor to maintain the internal surfaces of the conveyor at a low temperature. One suitable and desirable method is to provide a water jacket about the conveyor with water being continuously circulated through the jacket. The energy values in the hot effluent water can be recovered in the meat processing plant or drier if desired. The benefits of a jacketed screw fed conveyor are the positive drive feed, enabling supply to continue even if some of the material should inadvertently stick to the walls of the conveyor, and enabling a wider choice of materials for the construction of the conveyor and the jacket, for example stainless steel can be used. The screw feed outlet is designed to deliver the feedstock into the central portion of the hot zone and it is desirable for this purpose for the conveyor to enter the dryer through the side wall of the combustion chamber, as illustrated in Figures 1 and 2. The feed material is adapted to fall within the hot zone 6 and move in the direction of arrow A within the drying cylinder. The hot zone and the cooler zone 10 are, as mentioned above, desirably one continuous rotating cylinder being rotated by a suitable motor (not shown), the speed of which is variable. The residence time of the feedstock in the hot zone is for a period sufficient for fine hair and wool residues to be flashed off along with much of the surface moisture but not long enough to denature the protein material to any great extent. The residence time can be varied by varying the slope of the floor of the hot zone, and varying the speed of rotation of the cylinder. The slope of the floor 22 in the hot zone is important. If the slope is too slight then when the feedstock is being supplied at a high rate, backflow can occur towards the combustion chamber which can lead to ignition and disastrous fires. If the slope is too steep the benefit of the hot zone treatment can be lost such as inadequate flashing of hair residues and surface moisture. The presently employed slope of the hot zone is such that the angle α in Figure 1 is about 6 o . In addition to give a positive thrust to forward movement baffles can be provided which need not be too prominent. For example as shown in Figures 1, 2 and 3 a helical rib 23 can be provided of one or two starts. The slope of the floor in the cooler zone 10 is less than that in the hot zone 10. The angle of inclination of the lower temperature area 10 is slight as the residence time in this part of the chamber is designed to be preferably from 15 to 45 minutes. An angle of less than 1 o is desired and the currently employed slope is about 0.63 o . The whole cylinder is desirably insulated as much as possible to prevent heat losses and hence conserve energy. The output from the cylinder feeds into a hopper and thence through discharge valve 17 where it can be packed off into suitable containers. Exhaust gases from the cylinder pass out through outlet 12 where they can all, or part be recycled with part being fed through dehumidifiers for return to the combustion chamber 1. At the outlet end 11 a temperature sensor is provided to measure the temperature of the exhaust gases. This temperature is designed to be 110 o C ±5 o C, more preferably ± 2 o C. If the temperature varies from this amount then a signal is generated to vary the supply of the fuel (e.g. natural gas) to the flame in the combustion chamber. This is designed to give a product with a moisture content of just less than 8%. If a lower moisture content is desired then the outlet sensor will be set to detect variations from a higher temperature. For example a sensor detecting variations from a temperature of 135 o C can yield a product with a moisture content of 1 1/2 - 2%. A temperature lower than 110 o C can be used where higher moisture contents are requried. When a new cylinder is commissioned a certain amount of experimentation will be necesary to ensure that a suitable flame size in conjunction with the velocity of the air through the combustion chamber and the rotation speed of the chamber provides the desired temperature gradient from the hot zone to the outlet end. Once such has been set then monitoring the outlet end temperature should be adequate to ensure that the hot zone temprature is satisfactory. Obviously other monitoring systems can be employed as well as discussed above. As shown in Figure 3 the internal surface of the rotating cylinder is provided with baffles 21, desirably positioned uniformly throughout the internal circumference of the cylinder. The baffles are designed to lift the feedstock continuously so that the feedstock is as much as possible falling within the cylinder. In this fashion it is exposed to the flow of heated air for the greatest time possible and thus increases the drying rate. As is shown in Figure 2 these baffles or flights 7 can extend the length of the cylinder. The cylinder is driven through a variable speed motor desirably through a suitable reduction gear box not shown. The cylinder is carried on suitable bearing rollers 19 and 20 (Figure 3) and a similar pair or pairs at necessary places along the length of the cylinder. These bearing rollers are adapted to rotate on a suitable spindle and bear against suitable support rings 8. In addition an annular flange 9 located adjacent the support rings engages against a thrust roller 18. The rotational speed will be chosen in combustion with the other parameters. One suitable speed is 6 RPM. The rotating cylinder is supported on a suitable support means such as a stand 14. The combustion chamber 1 is fixed and supported by a suitable support stand such as stand 13. The heating is desirably by burning a suitable flammable fuel such as natural gas within the combustion chamber which is open directly into the hot zone 6. However it is desired that no live flame actually contacts the feedstock. To ensure sufficient heat is transferred into the hot zone and into the cooler zone 10, air is forced through the flame in the combustion chamber at sufficient speed to generate the required temperature gradient throughout the apparatus. Any recycled exhaust gases are fed into the combustion chamber. Since combustion chamber 1 is fixed and the remainder of the drier is rotating suitable seals are provided at the junction 3 of the two units. Such a seal is not fluid tight but still allows only a minimum amount of ventilation. It is desirable to maintain the cylinder at a negative pressure in comparison to atmospheric so that the ventilation flow is from outside the cylinder into the cylinder. If the flow is in the reverse direction besides the heat loss, there is a potential dust problem created which can lead to flammability problems. The negative pressure is created by a suitable extractor fan in the outlet flue 12 but is at a minimum to avoid extraction of a significant amount of fines which would reduce the amount of recoverable product.

Claims: A method of drying damp organic material comprising the steps of: providing a drying chamber having an substantially horizontal axis, said drying chamber comprising a first zone (6) that has a truncated conical shape, the larger diameter end of which is downstream of the smaller diameter end and which is relatively short and a second zone (10) which is direct fluid communication with said first zone (6) and which is substantially cylindrical in shape and is relatively long; rotating said drying chamber about said axis, heating said first zone to a relatively high temperature and said second zone to a lower temperature; and supplying material to be dried to said first zone so as to fall onto the sloping inner surface thereof, the slope being such that the residence time in said first zone is relatively short, and the temperature within said hot zone is at least about 750°C so that surface moisture and organic surface residues on the damp material are flashed off without denaturing said material, the material passing from said first zone to said second zone where the residence time of the material is relatively long and said material is dried. A method as claimed in claim 1 in which the material is damp bone meal from a meat processing plant. A method as claimed in claim 1 or 2 in which the heat source is by direct heat transfer from a live flame. A method as claimed in any preceding claim in which gases from the exhaust are recycled for use in the heating source. A method as claimed in claim 4 in which the gases are split into two trains, one of which is returned directly to the heat source, the other of which is subject to dehumidification before return. A method as claimed in claim 5 in which the second stream is also cooled to increase the potential for rehumidification before returning to the heat source. A method as claimed in any preceding claim in which the outlet temperature is monitored by a temperature sensor adapted to modify the rate of evaporation of moisture from the damp product. A method as claimed in claim 7 in which the rate of evaporation is varied by varying the energy supply to the heat source. A method as claimed in any preceding claim in which the pressure within the chamber is kept below atmospheric.

Inventors: TAYLOR, ANDREW WHITFIELD
Applicants: PACIFIC PROTEINS LIMITED
Application year: 1985
Main classification: F26B11
IPC codes: F26B25, F26B11, F26B3