The present invention deals broadly with the field of processing granular material having a solvent entrained therein. More narrowly, however, it deals with equipments for removing solvent from a granular material, such as edible grains, where the solvent has been used to separate one portion of the grain from another. The specific focus of the invention is the construction of a desolventizer-toaster (DT) which affords various advantages over such equipments known in the prior art.
Various solvents such as hexane, heptane and different alcohols are commonly used for treating granular solid materials to facilitate separation of one portion of the granular material from another. Typically, the solvents are used in processing of edible grains, in order to separate, for example, oil of the grain from the meal. Typical of this processing is the extraction of soybean oil from soybean grain.
The typical soybean oil-extraction process includes numerous steps. By way of example, included are cleaning, cracking, conditioning, expelling and solvent extraction. Performance of these steps results in an oil-depleted meal and a liquid oil. The oil can be further refined and processed for use in the making of consumer products such as margarine and shortening.
The oil seed meal, on the other hand, can be used as animal feed. It will be understood, of course, that the meal must be worked to remove residual solvent prior to being used for this purpose. After the extraction of oil and/or fat from the soybeans, some residual solvent remains entrained or entrapped within the solids. In order to maximize usage of the solids, it is imperative that as much of the residual solvent as possible be removed.
Traditionally, the solids are heated under a slight vacuum, and the solvent is effectively boiled from the meal. This process is known as desolventizing or desolventizing/toasting.
An apparatus referred to as a DT is known in the art and used to remove residual solvent from granular material. A DT commonly takes the form of a cylindrical chamber having mounted centrally therewithin a rotary shaft which drives multiple agitators or sweep arms. The agitators move over the bottom of each of a plurality of typically vertically stacked compartments. Frequently, an agitator is, in fact, spaced a slight distance from the bottom surface of the compartment within which the agitator moves. Such a construction serves to maintain adequate mixing motion of the meal and to keep the flakes as loose as possible.
The meal flakes pass through apertures typically distributed uniformly over the area of the bottom of the particular compartment. Such a construction serves to ensure substantially uniform distribution of live steam introduced through the bottom of the compartment. The compartment bottom, in such an equipment, can be defined by two plates which enclose a steam space connected to a supply of steam.
DT's such as that described hereinbefore typically have a number of shortcomings. Accessibility to the compartments of the DT from the outside of the equipment can be difficult. Repairs in various locations of the DT can, therefore, be difficult. Repairs to condensate and steam lines can be quite slow. With such prior art equipment, downtime can be significant.
Conventional DT piping frequently includes multiple bends and welds. This deters expeditious repairing of problems and, therefore, maximizes downtime.
The manufacture of a structure in accordance with the present invention facilitates isolation of locations where leaks might occur if an equipment in accordance with the invention is provided with a threaded connection for egress of steam condensate. This construction facilitates hydro-testing. Conceivably, all expansion stress-related failures could be moved outside of the vessel.
Because of proximity to the outer rim of a compartment, reduction of difficulty of alignment that has created problems with the packing gland can be accomplished.
It is to these shortcomings of the prior art and to the favorable characteristics provided that the present invention is directed. It is a piping attachment for steam and condensate connections to DT trays. More specific features and advantages obtained in view of those features will become apparent with reference to the further discussion herein and accompanying drawing figures.
The present invention is a construction of a DT which facilitates introduction of live steam into chambers of the DT. The construction also facilitates egress of steam condensate from the chambers.
The invention comprises one or more attachments, which can be nipple-like in construction, each of which mates with one chamber port spaced angularly from the other ports in a DT chamber. The nipple-like construction renders the structure easily accessible. This is true because of the radially peripheral placement of the ports. The number of egress ports will vary depending upon the construction and application of the particular DT. Similarly, placement will vary depending upon the particular DT and its construction and application.
The invention is novel and unobvious in various contexts. It is viewed as a desolventizer/toaster (DT) which, as is the prior art structure illustrated in
In a preferred embodiment, the port passed through the wall defining the body. As will be able to be seen, such a construction renders the interior of the generally cylindrical body more accessible than is the case with the prior art.
In a preferred construction of the invention, one or more of the axially aligned chambers are, in turn, subdivided into a plurality of circumferentially coextensive plenums. Barriers, extending generally from the axis with respect to which the generally circularly cylindrical body of the DT is formed, thereby define a plurality of circumferentially coextensive plenums.
The various embodiments and anticipated variations are shown in the accompanying drawing figures. The present invention is illustrated in the drawing figures accompanying this text.
Referring now to the drawing figures, wherein like reference numerals denote like elements throughout the several views,
The vertical column 14 generally includes an upper indirect heating zone 30 and a lower direct heating zone 50. The upper indirect heating zone 30 includes five or less trays 18; four are shown in the drawing. In the upper indirect heating zone 30, the trays 18 are steam heated basket type trays which permits solvent vapors to flow around the trays at a low velocity and thereby minimize fines carried out of the column 14 with the solvent vapor. This provides a “clean” solvent vapor and thereby obviates the need for pretreatment prior to condensing of such solvent vapors.
The DT illustrated in
The present invention does, therefore, employ a design which affords the ability to easily access the interior of the housing 12 from outside of the vessel. Such accessibility enables facile repair of condensate and steam lines. It also enables isolation of locations where leaks might take place contrary to conventional piping with multiple bends. Threaded connections allow for hydro-testing and also provides added barrier and pipe positioning for critical lock-pipe weld coseal.
Location of components at the peripheral rim reduces alignment difficulties. Such difficulties have, in the past, created problems with a packing gland.
The present invention is thus an improved DT apparatus. It will be understood that this disclosure, in many respects, is only illustrative. Changes may be made in details, particularly in matters of shape, size, material, and arrangement of parts without exceeding the scope of the invention. Accordingly, the scope of the invention is as defined in the language of the appended claims.
This is a regular application filed under 35 U.S.C. §111(a) claiming priority, under 35 U.S.C. §119(e) (1), of provisional application Ser. No. 61/266,021, previously filed Dec. 2, 2009 under 35 U.S.C. §111(b).
Number | Date | Country | |
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61266021 | Dec 2009 | US |