US238531A - Said sohutte as - Google Patents

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US238531A
US238531A US238531DA US238531A US 238531 A US238531 A US 238531A US 238531D A US238531D A US 238531DA US 238531 A US238531 A US 238531A
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steam
air
exhauster
heater
boiler
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24DDOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D1/00Steam central heating systems

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  • HENRY SOHOLFIELD OF GUATEMALA, CENTRAL AMERICA, AND LOUIS SGHUTTE, OF PHILADELPHIA, PENNSYLVANIA; SAID SOHUTTE AS- SIGNOR TO SAID SOHOLFIELD.
  • Our invention relates to that class of drying apparatus wherein a body or receiver to hold the material is used in connection with a steam-jet exhauster to cause the passage of air through the body; and the invention consists in the combination of the steam-jet exhauster with a steam-radiator to heat the air, and a steam-boiler connected with both the exhauster and the radiator, whereby an automatic regulation of the temperature in the receiver is secured, as hereinafterdescribed, and in de tails which will be more fully explained.
  • the drawing represents an elevation of our improved apparatus, showing the casing or body in section.
  • the object of our invention is to provide means whereby granular or fibrous substances may be dried in bulk without agitation or stirring, and without dividing the mass into separate layers.
  • the casing or body with a perforated bottom or screen, to support the material and to permit air to enter and pass up through the same, and with atop or cover which may be closed air-tight, with the exception of a central openingcommunicating with thejet apparatus, the receiving space or chamber being free from obstructions of any kind.
  • a second screen is placed above the receiving-space.
  • the cover or top of the chamber is made air-tight, with the exception above noted, but is furnished with openings through which the material may be supplied, leveled, and compacted, as is also the upper screen when used.
  • the top and screen are both provided with means of closing the openings mentioned, the former being adapted to seal the top against the admission ofair.
  • the heater is preferably located directly beneath the receiving-chamber, in a downward extension of the casing, but may be placed elsewhere, provided it be made to communicate with said chamber by a closed trun k or passage.
  • the jet apparatus and the heater recelve steam from one and the same boiler.
  • A represents the body or casing, having a tight cover or top communicating by a central opening with a steam-jet exhauster, B, and provided with openings for the admission of the material to be treated, said openings being furnished with close-fitting covers or doorsf, by which to close them against the admission of air.
  • the casing or body is furnished with a wire screen or perforated bottom or diaphragm, 8, said casing being preferably extended below thesame, as shown, to form a chamber or housing for the heater 0, which consists of a steam-pipe coiled or carried back and forth therein, and, by preference, connecting at both ends with a steam-boiler, D, at different levels.
  • the drier with its heater, is mounted upon an elevated platform, E, in order that the water produced by condensation in the steam-heating pipe may flow back to the boiler.
  • valves 1) and 0 being furnished, to regulate the supply of steam to the two, respectively.
  • a second screen or perforated diaphragm, s, furnished with openings having covers f, is represented in the drawing directly above the space occupied bythe material to be treated, and thatadoor, a, closes an opening through the side of the casing or body A at the lower part of the receiving-chamber.
  • This screen is intended to prevent the air-current from carrying the material,when of a light or tibrous character, into the jet apparatus, while the door is designed to permit the removal of the contents of the chamber.
  • the apparatus being thus constructed and arranged, and the casing or housing of the heater being so mounted as to permit the free entrance of air from below, the operation is as follows:
  • the material or substance to be treated is supplied to thereceiving-chamber through the openings in the top, the door a being closed, and through the openings in the upper screen, if used, and is leveled, or, if necessary, compacted, in order that the interstices and spaces between the particles may be uniform throughout.
  • the covers are then applied and the valves 1) and 0 opened, thus admitting steam from the boiler D to the exhauster B and heater G simultaneously.
  • the exhauster B creates a suction through the central opening in the top of the casing, thereby drawing air upward through the mass of material in the receiving-chamber, said air entering at the bottom of the casing, passing upward in contact with the steam-heating pipes, and being thereby dried and heated, thence through the perforated bottom or screen and through the material, and finally out through the exhauster.
  • valves I) and 0 will be adjusted in start ing the apparatus so as to establish a certain general relation between the amount of steam passing to the heater and the amount supplied to the exhauster; but this may vary, and is not a matter of importance.
  • the amount of steam condensed in the heater will depend entirely upon the amount of air drawn through it, which acts as the condensing medium. If, now, the steam pressure should rise above the average, a greater volume of air will be drawn by the exhauster, and a consequently larger volume of air will have to be heated by the heater, thereby keeping its temperature the same as it was at normal steam-pressure, whereas if the volume of air drawn had remained the same as at normal steam-pressure, its temperature would have been increased and perhaps have injured the material treated. This heating of the increased volume of air has also the effect of increasing the consumption of steam in the heater, so that in a few minutes the steampressure will be brought to that point which can be maintained by the boiler.
  • ⁇ Ve are aware that air has been drawn through a body containing wheat by means of a steam-jet exhanster, and that it has been proposed to admit hot or cold air or steam directly into said body or receiver in contact with the grain, the means by which the air was to be heated not being stated.
  • Ourinvention relates to an apparatus wherein the air is heated by means of steam-radia tors, and in which the radiator and the ex haustin g apparatus are supplied with steam from their common source, and is confined to an apparatus wherein the steam is prevented from coming in direct contact with the grain or other material under treatment.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Drying Of Solid Materials (AREA)

Description

(No Model.)
11. SOHOLFIELD & L. SGHUTT'E.
Drying Apparatus.
Pate nted March 8,1881.
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N. PETERS. PHOTO-LITMOGRAPHER. WASHlNGTON, D C.
llwirno STATES ATENT rrreE.
HENRY SOHOLFIELD, OF GUATEMALA, CENTRAL AMERICA, AND LOUIS SGHUTTE, OF PHILADELPHIA, PENNSYLVANIA; SAID SOHUTTE AS- SIGNOR TO SAID SOHOLFIELD.
DRYING APPARATUS.
SPECIFICATION forming part of Letters Patent No. 238,531, dated March 8, 1881.
Application filed September 15, 1880. (No model.)
To all whom it may concern:
Beit known that we, HENRY SCHOLFIELD, of Guatemala, Central America, and LOUIS SOHUTTE. of Philadelphia, in the county of Philadelphia and State of Pennsylvania, have invented certain Improvements in Drying Apparatus, of which the following is a specification.
Our invention relates to that class of drying apparatus wherein a body or receiver to hold the material is used in connection with a steam-jet exhauster to cause the passage of air through the body; and the invention consists in the combination of the steam-jet exhauster with a steam-radiator to heat the air, and a steam-boiler connected with both the exhauster and the radiator, whereby an automatic regulation of the temperature in the receiver is secured, as hereinafterdescribed, and in de tails which will be more fully explained.
The drawing represents an elevation of our improved apparatus, showing the casing or body in section.
The object of our invention is to provide means whereby granular or fibrous substances may be dried in bulk without agitation or stirring, and without dividing the mass into separate layers.
To this end we construct the casing or body with a perforated bottom or screen, to support the material and to permit air to enter and pass up through the same, and with atop or cover which may be closed air-tight, with the exception of a central openingcommunicating with thejet apparatus, the receiving space or chamber being free from obstructions of any kind. When intended for operating upon light material, liable to be carried up by the draft of the air, a second screen is placed above the receiving-space. The cover or top of the chamber is made air-tight, with the exception above noted, but is furnished with openings through which the material may be supplied, leveled, and compacted, as is also the upper screen when used. The top and screen are both provided with means of closing the openings mentioned, the former being adapted to seal the top against the admission ofair. The
heater is preferably located directly beneath the receiving-chamber, in a downward extension of the casing, but may be placed elsewhere, provided it be made to communicate with said chamber by a closed trun k or passage. The jet apparatus and the heater recelve steam from one and the same boiler.
Referring to the drawing, A represents the body or casing, having a tight cover or top communicating by a central opening with a steam-jet exhauster, B, and provided with openings for the admission of the material to be treated, said openings being furnished with close-fitting covers or doorsf, by which to close them against the admission of air. The casing or body is furnished with a wire screen or perforated bottom or diaphragm, 8, said casing being preferably extended below thesame, as shown, to form a chamber or housing for the heater 0, which consists of a steam-pipe coiled or carried back and forth therein, and, by preference, connecting at both ends with a steam-boiler, D, at different levels. The drier, with its heater, is mounted upon an elevated platform, E, in order that the water produced by condensation in the steam-heating pipe may flow back to the boiler.
As will be seen by referring to the drawing, the jet apparatus or exhauster B and the hearerOconnect with the same boiler D, valves 1) and 0 being furnished, to regulate the supply of steam to the two, respectively.
It will also be observed thata second screen or perforated diaphragm, s, furnished with openings having covers f, is represented in the drawing directly above the space occupied bythe material to be treated, and thatadoor, a, closes an opening through the side of the casing or body A at the lower part of the receiving-chamber. This screen is intended to prevent the air-current from carrying the material,when of a light or tibrous character, into the jet apparatus, while the door is designed to permit the removal of the contents of the chamber.
If the apparatus be intended to operate only on granular substances, not liable to be carried ofi' by the air-current, the upper screen, 8,
may be omitted, though it will not in any way interfere with the action of the apparatus if retained.
The apparatus being thus constructed and arranged, and the casing or housing of the heater being so mounted as to permit the free entrance of air from below, the operation is as follows: The material or substance to be treated is supplied to thereceiving-chamber through the openings in the top, the door a being closed, and through the openings in the upper screen, if used, and is leveled, or, if necessary, compacted, in order that the interstices and spaces between the particles may be uniform throughout. The covers are then applied and the valves 1) and 0 opened, thus admitting steam from the boiler D to the exhauster B and heater G simultaneously. The exhauster B creates a suction through the central opening in the top of the casing, thereby drawing air upward through the mass of material in the receiving-chamber, said air entering at the bottom of the casing, passing upward in contact with the steam-heating pipes, and being thereby dried and heated, thence through the perforated bottom or screen and through the material, and finally out through the exhauster.
The valves I) and 0 will be adjusted in start ing the apparatus so as to establish a certain general relation between the amount of steam passing to the heater and the amount supplied to the exhauster; but this may vary, and is not a matter of importance.
In treating most substances, however, it is important that a certain temperature shall not be exceeded. To maintain uniformly the desired temperature automatically, and without in any way depending upon attendants, and under variations in the boiler-pressure and other changes liable to occur about the steamgenerating apparatus, we have arranged the parts as above described, supplying the exhaustin g device and the heater from the same boiler. The effect of this arrangement is a far more perfect regulation and control of the temperature than can be attained by any other means of which we are aware, as we will now explain.
The amount of steam condensed in the heater will depend entirely upon the amount of air drawn through it, which acts as the condensing medium. If, now, the steam pressure should rise above the average, a greater volume of air will be drawn by the exhauster, and a consequently larger volume of air will have to be heated by the heater, thereby keeping its temperature the same as it was at normal steam-pressure, whereas if the volume of air drawn had remained the same as at normal steam-pressure, its temperature would have been increased and perhaps have injured the material treated. This heating of the increased volume of air has also the effect of increasing the consumption of steam in the heater, so that in a few minutes the steampressure will be brought to that point which can be maintained by the boiler. It will thus be seen that the regulation of the temperature is entirely automatic, and that the effect of varying steam-pressure consequent upon the nature of the fuel, attention, or other causes will be compensated for simply in time of drying. The apparatus serves the same purpose also as would a safety-valve applied to the boiler.
It is apparent that the direction in which the air is made to travel, the form and construction of the heater and exhauster, and the materials employed in construction may be varied, that a blast may be employed instead of suction, and that other modifications of details may be made. The construction and arrangement shown and described is, however, preferred, and an exhauster of the well-known Korting type is found very efficient. Other forms of exhausting device operated by steam may, however, be employed.
\Ve are aware that air has been drawn through a body containing wheat by means of a steam-jet exhanster, and that it has been proposed to admit hot or cold air or steam directly into said body or receiver in contact with the grain, the means by which the air was to be heated not being stated.
Ourinvention relates to an apparatus wherein the air is heated by means of steam-radia tors, and in which the radiator and the ex haustin g apparatus are supplied with steam from their common source, and is confined to an apparatus wherein the steam is prevented from coming in direct contact with the grain or other material under treatment.
Having thus described our invention, what we claim is 1. The combination of a body or receiver, a steam-jet apparatus to produce acurrentof air through the same, a steam-radiator to heat the air entering the body, and a steam-boiler connected with both the exhauster and the radiator, whereby an automatic regulation of the temperature in the body is secured.
2. The combination of the body or receiver, the jet-exhauster at its top, the steam-radiator in its base, and the steam-generator connected with both the exhauster and the radiator.
HENRY SOHOLFIELD. LOUIS SOHUTTE. Witnesses CHARLES W. OoULs'roN, WILLIAM ROYAL.
IIO
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