US789807A - Apparatus for cooling and drying granular materials. - Google Patents

Apparatus for cooling and drying granular materials. Download PDF

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US789807A
US789807A US21054104A US1904210541A US789807A US 789807 A US789807 A US 789807A US 21054104 A US21054104 A US 21054104A US 1904210541 A US1904210541 A US 1904210541A US 789807 A US789807 A US 789807A
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cooling
walls
granular materials
drying
plates
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US21054104A
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Franz Holl
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B7/00Combinations of wet processes or apparatus with other processes or apparatus, e.g. for dressing ores or garbage

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  • This invention relates to an apparatus for cooling and drying granular materials, such as moist sugar and the like.
  • the apparatus is constructed in such a manner that the material is first passed through a sifting-drum and then traverses the apparatus from top to bottom zigzag, being continuously exposed to a current of fresh air. If the apparatus is to be used for drying excessively-moist material, steam-pipe coils may be inserted in the apparatus.
  • FIG. 2 is a side view of the cooling-tower without the outer casing.
  • the apparatus is inclosed in a casing a, which has two openings Z) 7) opposite each other for the admittance of outer air.
  • the drying apparatus proper is inclosed, which consists of a tower, suitably of rectangular cross-section.
  • the tower is composed of two solid walls 0 of wood or any other material which is a bad heat-conductor, and of two walls made of laths which are fixed with both ends to the walls 0 c at a certain distance from each other.
  • two vertical partition-walls d d are arranged, which are composed of cross-laths standing opposite the intervals between the laths CZ.
  • bafiie-plates e To the laths (Z and d bafiie-plates e are linked. In each set the baffle-plates are interconnected by means of rod 0 or 19, respectively, so that the position of the baffle-plates of each set can be adjusted according to requirement.
  • distributing-rollers 7c are rotatably mounted in the upper end of the cooling-tower.
  • a rectangular cover-plate w is fixed, which serves as a guide for the material to be dried.
  • a feeding-channel f is fixed to the inner surface of the top plate of casing a.
  • a rotary sieve h is mounted in said feeding-channel, and a funnel g is provided in the top plate of the apparatus, through which funnel the material to be dried is fed into the rotary sieve.
  • guide-plates z' t" are fixed, which lead the material to be dried onto the distributing-rollers 7t 71;.
  • An aspirator Z arranged outside the apparatus, is connected with the drying-tower by a suction-pipe m. p,
  • the apparatus operates as follows: The granular material to be dried is fed through the funnel g onto the rotary sieve h, whereby the lumps are separated. The sifted material-su gar or the likeis transported through the rotary sieve onto the rectangular top wall and guided by the same and the guide-plates 0 onto the distributing-rollers 76 7c. The material now passes from one baffle-plate e to the other down to the bottom of the apparatus. A continuous current of air is produced in the apparatus by the aspirator, to which the material is exposed. The thickness of the flow of material can be varied by adjusting the position of the bafiie-plates.
  • An apparatus for drying and cooling granular material such as moist sugar comprising in combination with the outer casing provided with openings for the admittance of the outer air a vertical drying-tower consisting of two solid walls of wood and of two walls made of cross-laths arranged at a uniform distance apart, two inner vertical partition-walls parallel with said outer lath walls consisting of laths placed at the intervals of the laths of the outer walls, bafiie-plates hinged with one end to the inner surface of the outer and inner laths, means for adjusting the position of said baffle-plates, a rectangular top plate fixed to the upper ends of the inner lath walls, two distributing-rollers rotatably mounted below the lower edges of said rectangular top plate, a feeding-channel projecting from the top plate of the casing, a rotary sieve rotatably mounted in said channel, guide-plates fixed to the lower edges of the two opposite Walls

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  • Drying Of Solid Materials (AREA)

Description

PATENTED MAY 16, 1905.
P. HOLL.
APPARATUS FOR COOLING AND DRYING GRANULAR MATERIALS.
APPLICATION FILED MAY 31,1904.
Zita??? ill! \l A rlllllllllfllllllfll J12 2/60? for! Franz ][0 Z 5 UNTTen STATES Patented May 16, 1905.
PATENT FRANZ HOLL, OF WVORMS, GERMANY.
SPECIFICATION forming part of Letters Patent No. 789,807, dated May 16, 1905.
Application filed May 31 1904:. Serial No. 210,541.
i 0 all whom it may concern:
Be it known that I, FRANZ How, a subject of the German Emperor, and a resident of WVorms-on-the-Rhine, Germany, have invented new and useful Improvements in Apparatus for Drying Granular Materials, such as Moist Sugar and the Like, of which the following is a specification.
This invention relates to an apparatus for cooling and drying granular materials, such as moist sugar and the like. The apparatus is constructed in such a manner that the material is first passed through a sifting-drum and then traverses the apparatus from top to bottom zigzag, being continuously exposed to a current of fresh air. If the apparatus is to be used for drying excessively-moist material, steam-pipe coils may be inserted in the apparatus.
In the accompanying drawings the improved apparatus is shown in Figure l in a vertical section. Fig. 2 is a side view of the cooling-tower without the outer casing.
As can be seen from the drawings, the apparatus is inclosed in a casing a, which has two openings Z) 7) opposite each other for the admittance of outer air. In this casing 60 the drying apparatus proper is inclosed, which consists of a tower, suitably of rectangular cross-section. The tower is composed of two solid walls 0 of wood or any other material which is a bad heat-conductor, and of two walls made of laths which are fixed with both ends to the walls 0 c at a certain distance from each other. In the cooling-tower two vertical partition-walls d d are arranged, which are composed of cross-laths standing opposite the intervals between the laths CZ. To the laths (Z and d bafiie-plates e are linked. In each set the baffle-plates are interconnected by means of rod 0 or 19, respectively, so that the position of the baffle-plates of each set can be adjusted according to requirement.
In the upper end of the cooling-tower, between the outer and inner lath walls d d, distributing-rollers 7c are rotatably mounted. On the upper end of the inner partition-walls d d a rectangular cover-plate w is fixed, which serves as a guide for the material to be dried.
A feeding-channel f is fixed to the inner surface of the top plate of casing a. A rotary sieve h is mounted in said feeding-channel, and a funnel g is provided in the top plate of the apparatus, through which funnel the material to be dried is fed into the rotary sieve. At the two side walls of the feedingchannel f,-which run parallel with the lath walls d d, guide-plates z' t" are fixed, which lead the material to be dried onto the distributing-rollers 7t 71;.
An aspirator Z, arranged outside the apparatus, is connected with the drying-tower by a suction-pipe m. p,
The apparatus operates as follows: The granular material to be dried is fed through the funnel g onto the rotary sieve h, whereby the lumps are separated. The sifted material-su gar or the likeis transported through the rotary sieve onto the rectangular top wall and guided by the same and the guide-plates 0 onto the distributing-rollers 76 7c. The material now passes from one baffle-plate e to the other down to the bottom of the apparatus. A continuous current of air is produced in the apparatus by the aspirator, to which the material is exposed. The thickness of the flow of material can be varied by adjusting the position of the bafiie-plates.
Having fully described my invention, what I claim, and desire to secure by Letters Patent, is- I An apparatus for drying and cooling granular material such as moist sugar, comprising in combination with the outer casing provided with openings for the admittance of the outer air a vertical drying-tower consisting of two solid walls of wood and of two walls made of cross-laths arranged at a uniform distance apart, two inner vertical partition-walls parallel with said outer lath walls consisting of laths placed at the intervals of the laths of the outer walls, bafiie-plates hinged with one end to the inner surface of the outer and inner laths, means for adjusting the position of said baffle-plates, a rectangular top plate fixed to the upper ends of the inner lath walls, two distributing-rollers rotatably mounted below the lower edges of said rectangular top plate, a feeding-channel projecting from the top plate of the casing, a rotary sieve rotatably mounted in said channel, guide-plates fixed to the lower edges of the two opposite Walls of the channel parallel to the lath Walls and an aspirator connected With the cooling-tower by a suction-pipe, substantially as described and shown and for the purpose set forth.
In testimony whereof I have hereunto set my hand in presence of tWo subscribing Witnesses.
FRANZ HOLL'.
Witnesses:
H. W. HARRIS, J ACOB ADRIAN.
US21054104A 1904-05-31 1904-05-31 Apparatus for cooling and drying granular materials. Expired - Lifetime US789807A (en)

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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2697881A (en) * 1950-12-22 1954-12-28 Phillips Petroleum Co Means for displacing hydrocarbon vapors from a fluidized spent catalyst
US2799097A (en) * 1953-12-03 1957-07-16 French Oil Mill Machinery Cooling of hot particles such as hot meal
US3092471A (en) * 1959-11-20 1963-06-04 George F Ropes Process for conditioning carbonaceous material
US3108448A (en) * 1960-01-07 1963-10-29 John R Hightower Method of cooling cement mixes for concrete
US3749549A (en) * 1972-01-31 1973-07-31 B Henderson Continuous heating apparatus for granular material
US4299598A (en) * 1976-03-24 1981-11-10 Dutkiewicz Ryszard K Panel gas filter for limestone dust
EP0514324A2 (en) * 1991-05-17 1992-11-19 HILTI Aktiengesellschaft Cooling apparatus
US5233766A (en) * 1992-06-05 1993-08-10 Frederiksen Wilfred C Vertical grain dryer

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2697881A (en) * 1950-12-22 1954-12-28 Phillips Petroleum Co Means for displacing hydrocarbon vapors from a fluidized spent catalyst
US2799097A (en) * 1953-12-03 1957-07-16 French Oil Mill Machinery Cooling of hot particles such as hot meal
US3092471A (en) * 1959-11-20 1963-06-04 George F Ropes Process for conditioning carbonaceous material
US3108448A (en) * 1960-01-07 1963-10-29 John R Hightower Method of cooling cement mixes for concrete
US3749549A (en) * 1972-01-31 1973-07-31 B Henderson Continuous heating apparatus for granular material
US4299598A (en) * 1976-03-24 1981-11-10 Dutkiewicz Ryszard K Panel gas filter for limestone dust
EP0514324A2 (en) * 1991-05-17 1992-11-19 HILTI Aktiengesellschaft Cooling apparatus
EP0514324A3 (en) * 1991-05-17 1993-09-01 Hilti Aktiengesellschaft Cooling apparatus
US5233766A (en) * 1992-06-05 1993-08-10 Frederiksen Wilfred C Vertical grain dryer

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