US1148331A - Furnace for heating gases or the like. - Google Patents

Furnace for heating gases or the like. Download PDF

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Publication number
US1148331A
US1148331A US83925414A US1914839254A US1148331A US 1148331 A US1148331 A US 1148331A US 83925414 A US83925414 A US 83925414A US 1914839254 A US1914839254 A US 1914839254A US 1148331 A US1148331 A US 1148331A
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chamber
furnace
sand
gases
hopper
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US83925414A
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Carl Martin Tage Olsson
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1836Heating and cooling the reactor
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28CHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
    • F28C3/00Other direct-contact heat-exchange apparatus
    • F28C3/10Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material
    • F28C3/12Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material the heat-exchange medium being a particulate material and a gas, vapour, or liquid
    • F28C3/14Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material the heat-exchange medium being a particulate material and a gas, vapour, or liquid the particulate material moving by gravity, e.g. down a tube

Definitions

  • This invention is for improvements in or relating to furnaces for heating gases and the like of the type in which the gases are passed through a stream of hot solid bodies, for example particles of sand and are heated thereby.
  • the apparatus for this purpose comprised a slightly inclined rotating drum communieating with a shaft at the lower end and a furnace at the upper end. Air and gas were fed into the shaft and, burning in the drum, passed out by the furnace. The material being treated was fed into the furnace and through the drum into the shaft; it absorbed heat from the hot products of combustion inthe furnace and from the flame in the drum, and gave up some heat to the air or gas in the shaft prior to its being burnt; it
  • apparatus for heating gases comprises a chamber, means for continuously feeding a stream of solid bodies into the top of it whence they fall to the bottom, means for supplying a continuous flow of hot gases to the bottom of the chamber and drawing them off at the top, a second chamber situated at a lower level than the first, a conduit conducting the stream of hot solid bodies from the bottom of the first chamber to the top of the second chamber so that it can fall to the bottom, and means for supplying a continuous flow of the gases to be heated to the bottom of the second chamber and means for drawing such gases off at the top.
  • a hopper or receptacle may be provided between the upper and lower chambers to intercept the flow of the sand or the like in its passage into the lower chamber, and its delivery end is so dimensioned relatively to the flow of the sand that the hopper is maintained partially filled with sand during the operation of the furnace and constitutes a seal against the escape of gas therethrough; this hopper may be provided with valves for regulating the flow of the sand through it so that when starting the apparatus the outlet can be closed to allow the hopper to be filled, the rate of the inflow and outflow of sand being maintained equal.
  • the furnace comprises -a vertical shaft or tower A, divided by a partition B into upper and lower chambers C C Each of these chambers is provided with a checker;
  • an opening E in the form of a hopper, the upper end of the opening E extending to the full dimensions of the chamber C and the lower end of it being suitably restricted to allow the correct quantity of flow of sand through the furnace.
  • a valve E may be provided within the hopper E to control the rate of flow of sand through it if it is so desired.
  • the chamber C has the bottom tapered and a screw conveyer F is disposed at the bottom.
  • Other conveyers F F and an elevator F convey the sand to the top of the chamber C again into which it is fed and distributed by a screw conveyer F.
  • Ordinary or silica sand may be suittheir heat to the sand falling speed of the conveyors and elevator is adjusted as required and the opening in the hopper E is simultaneously adjusted.
  • the outlet G at the top of the chamber 0 The air or gas which is to be heated is introduced at the bottom of the chamber C y a passage H and it passes upward absorbing heat from the hot sand which is falling downward. When fully heated it is withdrawn by the passage H at the top I of the chamber C
  • the hopper E is so 7 designed that a quantity of sand is mainso that there is no fear of the gases becom tained in it thereby providing a seal between the upper and lower chambers C C ing intermixed.
  • the furnace may be lined with suitable heat conserving material and it will be apto provide heat for the sand;
  • products of the electric furnace such as carborundum silundum, alundum or the like may be employed, these materials being of course pulverized or ground to provide particles of a suitable size.
  • the sand may be heated by waste gas from another furnace or fuel may be burned with air at the lower part of the chamber C if gaseous or liquid fuel is used a separate combustion chamber may be employed to insure'that the flame attains its maximum temperature before it comes into contact with the sand.
  • This apparatus may be used for heating air or gas for any purpose, thus in a process for the direct reduction of iron ore by a reducing gas, this gas may be conveniently raised to any desired temperature by this apparatus.
  • the gases passing ofl by the outlet G may, if all the heat has not been abstracted, be used for various purposes, such as heating water, or heating air supplied to other furnaces for combustion, but these do not constitute part of the present invention.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Furnace Details (AREA)

Description

C. M. ,T.- OLSSON.
FURNACE FOR HEATING GASES OR THE LIKE.
APPLICATION FILED MAY 18, 1914.
LM8L v Patented July 27, 1915.
ZLWSSGS.
CARL MARTTN TAGE OLSSON, OF SALTSJ'fiBADE-N, SWEDEN.
FURNACE IE OR HEATING GASES OR THE LIKE.
Specification of Letters Patent.
Patented July 27, 1915.
Application filed May 18, 1914. Serial No. 839,254.
To all whom, it may concern:
Be it known that I, CARL MARTIN TAGE ()LssoN, a subject of the King of Sweden, residing in the municipality of Saltsjiibaden, Sweden, have invented certain new and useful Improvements in Furnaces for Heating Gases or the like, of which the following is a specification.
This invention is for improvements in or relating to furnaces for heating gases and the like of the type in which the gases are passed through a stream of hot solid bodies, for example particles of sand and are heated thereby.
It has previously been proposed to heat air or other gases.by passing it through a chamber provided with horizontal partitions and channels in the walls of the chamber providing communication from one side of each partition to the other, the air being passed horizontally between each pair of partitions in turn; the partitions were perforated and hot sand was fed through the various partitions thus passing transversely across the flow of air to be heated. It has also been proposed to recover heat that would otherwise be wasted, in calcining ores or burning cement by' imparting it to the air supplied to the combustion chamber.
The apparatus for this purpose comprised a slightly inclined rotating drum communieating with a shaft at the lower end and a furnace at the upper end. Air and gas were fed into the shaft and, burning in the drum, passed out by the furnace. The material being treated was fed into the furnace and through the drum into the shaft; it absorbed heat from the hot products of combustion inthe furnace and from the flame in the drum, and gave up some heat to the air or gas in the shaft prior to its being burnt; it
will be seen that with this apparatus the air or gas is only heated on its way to the combustion chamber of the same apparatus, whereas the present invention provides for heating gases which may then be drawn ofl' hot and used for any other purpose. According to the present invention apparatus for heating gases comprises a chamber, means for continuously feeding a stream of solid bodies into the top of it whence they fall to the bottom, means for supplying a continuous flow of hot gases to the bottom of the chamber and drawing them off at the top, a second chamber situated at a lower level than the first, a conduit conducting the stream of hot solid bodies from the bottom of the first chamber to the top of the second chamber so that it can fall to the bottom, and means for supplying a continuous flow of the gases to be heated to the bottom of the second chamber and means for drawing such gases off at the top.
A hopper or receptacle may be provided between the upper and lower chambers to intercept the flow of the sand or the like in its passage into the lower chamber, and its delivery end is so dimensioned relatively to the flow of the sand that the hopper is maintained partially filled with sand during the operation of the furnace and constitutes a seal against the escape of gas therethrough; this hopper may be provided with valves for regulating the flow of the sand through it so that when starting the apparatus the outlet can be closed to allow the hopper to be filled, the rate of the inflow and outflow of sand being maintained equal.
The accompanying drawing is an elevation in section of a furnace in accordance with the present invention.
The furnace comprises -a vertical shaft or tower A, divided by a partition B into upper and lower chambers C C Each of these chambers is provided with a checker;
work of bricks D by which the fall of sand through the chambers is to a certain extent impeded. These bricks are tapered on their upper side so that no resting place is provided on which sand could lodge or collect.
In the partition B there is provided an opening E in the form of a hopper, the upper end of the opening E extending to the full dimensions of the chamber C and the lower end of it being suitably restricted to allow the correct quantity of flow of sand through the furnace. A valve E may be provided within the hopper E to control the rate of flow of sand through it if it is so desired.
The chamber C has the bottom tapered and a screw conveyer F is disposed at the bottom. Other conveyers F F and an elevator F convey the sand to the top of the chamber C again into which it is fed and distributed by a screw conveyer F. It will be seen that by this arrangement the sand in the'furnace is in constant circulation and a uniform rate of flow is maintained. If it is desired to change this. rate of flow, the
gases. Ordinary or silica sand may be suittheir heat to the sand falling speed of the conveyors and elevator is adjusted as required and the opening in the hopper E is simultaneously adjusted.
While the sand is passing through the chamber 0 it is heated by hot gases entering by passages G at the bottom of this chamber, these gases being any suitable hot productsof combustion. These gases pass upward through the chamber C giving up downward andthey are discharged, when cooled, by
' the outlet G at the top of the chamber 0 The air or gas which is to be heated is introduced at the bottom of the chamber C y a passage H and it passes upward absorbing heat from the hot sand which is falling downward. When fully heated it is withdrawn by the passage H at the top I of the chamber C As mentioned above the hopper E is so 7 designed that a quantity of sand is mainso that there is no fear of the gases becom tained in it thereby providing a seal between the upper and lower chambers C C ing intermixed.
The furnace may be lined with suitable heat conserving material and it will be apto provide heat for the sand;
able in most cases but if they are unsuitable, products of the electric furnace, such as carborundum silundum, alundum or the like may be employed, these materials being of course pulverized or ground to provide particles of a suitable size.
Various modifications may be made in the general arrangement of such furnaces according to this invention. Thus for example the sand may be heated by waste gas from another furnace or fuel may be burned with air at the lower part of the chamber C if gaseous or liquid fuel is used a separate combustion chamber may be employed to insure'that the flame attains its maximum temperature before it comes into contact with the sand.
This apparatus may be used for heating air or gas for any purpose, thus in a process for the direct reduction of iron ore by a reducing gas, this gas may be conveniently raised to any desired temperature by this apparatus. The gases passing ofl by the outlet G may, if all the heat has not been abstracted, be used for various purposes, such as heating water, or heating air supplied to other furnaces for combustion, but these do not constitute part of the present invention.
It has heretofore been proposed in the manufacture of iron to allow the ore to fall through a tower, in the upper part of which it is heated and in the lower part of which it is subjected to a reducing gas to deoxidize the ore but the present invention has for its object to provide an improved form of furnace for heating air or other gases which may subsequentl be applied to any desired purpose being i necessary uncontaminated with any products of combustion.
What I claim as my invention and desire I to secure by Letters Patent is In apparatus for heating gases the combination of a chamber, a conduit for supplying a continuous flow of hot gases to the bottom of said chamber and a conduit for drawing ofi these gases from the top, means for supplying a constant stream of solid bodies such as sand to the top of said chamber, a second chamber situated at a lower level than the first chamber, a conduit for supplying a continuous flow of gases to be heated to the bottom of said second chamber, a conduit for drawing them oil at the top thereof, a hopper in the bottom of the first chamber having 'a discharge opening into the top of the second chamber, a valve in said hopper controlling the flow of the solid bodies from the first chamber to the second chamber and constituting with them a seal against the escape of gas through the hopper, substantially as set forth.
In testimony whereof I have signed my name to this specification in the presence of two subscribing witnesses.
CARL MARTIN TAGE OLSSON.
H. D. J amison.
US83925414A 1914-05-18 1914-05-18 Furnace for heating gases or the like. Expired - Lifetime US1148331A (en)

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Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2417049A (en) * 1943-10-18 1947-03-11 Babcock & Wilcox Co Control system
US2422791A (en) * 1945-07-30 1947-06-24 Universal Oil Prod Co Endothermic catalytic conversion of hydrocarbons
US2443210A (en) * 1943-12-20 1948-06-15 Phillips Petroleum Co Quenching of hot gases
US2446388A (en) * 1943-10-20 1948-08-03 Brassert & Co Preheating furnace blast
US2447306A (en) * 1943-09-16 1948-08-17 Babcock & Wilcox Co Fluid heater
US2468712A (en) * 1944-12-21 1949-04-26 Babcock & Wilcox Co Heat exchanger
US2475255A (en) * 1944-03-17 1949-07-05 Standard Oil Dev Co Method of drying gases
US2512442A (en) * 1945-10-31 1950-06-20 Babcock & Wilcox Co Solid material heating apparatus
US2533142A (en) * 1945-07-19 1950-12-05 Pickands Mather & Co Heat-treating solids
US2556430A (en) * 1945-04-21 1951-06-12 Pure Oil Co Method and apparatus for preparing mixed sulfur-hydrocarbon vapors
US2571749A (en) * 1944-07-04 1951-10-16 Babcock & Wilcox Co Fluid heating
US2582116A (en) * 1948-08-24 1952-01-08 Phillips Petroleum Co Pebble heater chamber design
US2625377A (en) * 1948-12-28 1953-01-13 Phillips Petroleum Co Pebble chamber
US2662003A (en) * 1946-04-08 1953-12-08 Phillips Petroleum Co Process for effective catalytic conversion of hydrocarbons
DE920488C (en) * 1943-10-18 1954-11-22 Babcock & Wilcox Co Method and device for regulating the heating of an agent in a heater
DE972335C (en) * 1944-04-19 1959-07-02 Demag Ag Process and device for utilizing the sensible heat of useful gas from gas generators
US2946569A (en) * 1953-06-18 1960-07-26 Babcock & Wilcox Co Apparatus for cleaning the surfaces of heat exchange means
US2967693A (en) * 1956-08-31 1961-01-10 Air Preheater Pellet type heat exchanger
DE974985C (en) * 1943-09-16 1961-06-22 Babcock & Wilcox Co Process for heating a liquid or gaseous medium with the aid of a stream of a refractory, heat-transferring, solid material
US3061194A (en) * 1958-07-09 1962-10-30 Hazen Engineering Company Two-stage system for preheating combustion air

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE974985C (en) * 1943-09-16 1961-06-22 Babcock & Wilcox Co Process for heating a liquid or gaseous medium with the aid of a stream of a refractory, heat-transferring, solid material
US2447306A (en) * 1943-09-16 1948-08-17 Babcock & Wilcox Co Fluid heater
US2417049A (en) * 1943-10-18 1947-03-11 Babcock & Wilcox Co Control system
DE920488C (en) * 1943-10-18 1954-11-22 Babcock & Wilcox Co Method and device for regulating the heating of an agent in a heater
US2446388A (en) * 1943-10-20 1948-08-03 Brassert & Co Preheating furnace blast
US2443210A (en) * 1943-12-20 1948-06-15 Phillips Petroleum Co Quenching of hot gases
US2475255A (en) * 1944-03-17 1949-07-05 Standard Oil Dev Co Method of drying gases
DE972335C (en) * 1944-04-19 1959-07-02 Demag Ag Process and device for utilizing the sensible heat of useful gas from gas generators
US2571749A (en) * 1944-07-04 1951-10-16 Babcock & Wilcox Co Fluid heating
US2468712A (en) * 1944-12-21 1949-04-26 Babcock & Wilcox Co Heat exchanger
US2556430A (en) * 1945-04-21 1951-06-12 Pure Oil Co Method and apparatus for preparing mixed sulfur-hydrocarbon vapors
US2533142A (en) * 1945-07-19 1950-12-05 Pickands Mather & Co Heat-treating solids
US2422791A (en) * 1945-07-30 1947-06-24 Universal Oil Prod Co Endothermic catalytic conversion of hydrocarbons
US2512442A (en) * 1945-10-31 1950-06-20 Babcock & Wilcox Co Solid material heating apparatus
US2662003A (en) * 1946-04-08 1953-12-08 Phillips Petroleum Co Process for effective catalytic conversion of hydrocarbons
US2582116A (en) * 1948-08-24 1952-01-08 Phillips Petroleum Co Pebble heater chamber design
US2625377A (en) * 1948-12-28 1953-01-13 Phillips Petroleum Co Pebble chamber
US2946569A (en) * 1953-06-18 1960-07-26 Babcock & Wilcox Co Apparatus for cleaning the surfaces of heat exchange means
US2967693A (en) * 1956-08-31 1961-01-10 Air Preheater Pellet type heat exchanger
US3061194A (en) * 1958-07-09 1962-10-30 Hazen Engineering Company Two-stage system for preheating combustion air

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