US2874482A - Drying of moist material - Google Patents

Drying of moist material Download PDF

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US2874482A
US2874482A US448683A US44868354A US2874482A US 2874482 A US2874482 A US 2874482A US 448683 A US448683 A US 448683A US 44868354 A US44868354 A US 44868354A US 2874482 A US2874482 A US 2874482A
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temperature
belt
drying
radiation
heating
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Haltmeier Alfred
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Bayer AG
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B5/00—Drying solid materials or objects by processes not involving the application of heat
    • F26B5/04—Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum
    • F26B5/041—Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum for drying flowable materials, e.g. suspensions, bulk goods, in a continuous operation, e.g. with locks or other air tight arrangements for charging/discharging
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
    • F26B17/02—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by belts carrying the materials; with movement performed by belts or elements attached to endless belts or chains propelling the materials over stationary surfaces
    • F26B17/023—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by belts carrying the materials; with movement performed by belts or elements attached to endless belts or chains propelling the materials over stationary surfaces the material being a slurry or paste, which adheres to a moving belt-like endless conveyor for drying thereon, from which it may be removed in dried state, e.g. by scrapers, brushes or vibration
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00—Drying solid materials or objects by processes involving the application of heat
    • F26B3/28—Drying solid materials or objects by processes involving the application of heat by radiation, e.g. from the sun
    • F26B3/283—Drying solid materials or objects by processes involving the application of heat by radiation, e.g. from the sun in combination with convection
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00—Drying solid materials or objects by processes involving the application of heat
    • F26B3/28—Drying solid materials or objects by processes involving the application of heat by radiation, e.g. from the sun
    • F26B3/30—Drying solid materials or objects by processes involving the application of heat by radiation, e.g. from the sun from infrared-emitting elements
    • F26B3/305—Drying solid materials or objects by processes involving the application of heat by radiation, e.g. from the sun from infrared-emitting elements the infrared radiation being generated by combustion or combustion gases

Definitions

  • the present invention relates to an improved method of, and apparatus for, drying material on a belt drier by radiation.
  • An indication of the amount of moisture still remaining in the material being dried is given by the temperature of the material at the end of the radiation drying zone;
  • this temperature may, for example, be determined by means of thermometers, protected against the radiation, which contact the belt at this position. The more this final temperature exceeds the temperature at which the moisture evaporates from the material being dried,-the less is the amount of moisture remaining; it'is thus possible to take advantage of the temperatures of the dried material at the end of the radiation zone for regulating the amount of residual moisture in the undried material. If the material is dried under reducedpressur'e, the temperature at which the moisture evaporates depends on the pressure used.
  • present invention provides a method ofdrying moist material by spreading the moist material on the belt of a belt drier and drying the material by radiation, wherein .the moist material on the belt is pre-heated or pre-cooled and the resulting variations in temperature of the material are used to control the amount of radiated heat supplied to the material to dry it.
  • This preheating and/ or precooling of the moist material is referred to in the claims as' thermally varying the temperature of the moist material.
  • These variations in the temperature of the moist material spread on the belt may be obtained either by heating by preliminary irradiation or by a current of vapour being blown thereon, or by cooling by blowing on air.
  • the amount of radiated-heat supplied may be controlled by the variations in temperature of the heated or cooled material in various ways. If the rate at which radiated heat is supplied to the moist material is kept constant for a time, the material is heated more as its heat capacity 2,874,482 Patented Feb. 24, 1959 moist material is spread. If the rate of Preliminary heating or preliminary cooling is kept constant for a time, the rise or fall thus produced in the temperature of the material on the belt may be used to control the rate at which radiation energy is supplied to the drying zone, for ex-' ample by using electrical or perhaps pneumatic transmission devices to supply to the radiation heaters an amount of fuel or electric power which is proportional to the rise or fall in the temperature of the moist material resulting from the pre-heating or pre-cooling.
  • Controlling impulses may be supplied by temperature governors or difierential governors; these impulses may then be used simultaneously to regulate the pre-heating or pro-cooling of the material and to control the radiation to be subsequently used for drying purposes. Owing to the high thermal inertia of heating systems operated with gas, oil or elec tricity, it is possible to operate with simple limiting contact regulators. a
  • Thermal impulse emitters such as thermo-elements, resistanee thermometers or contact thermometers, arranged to slideon the, belt. or total radiation pyrometers if the layer of material is not to be damaged, are arranged between the pro-heating or pre-cooling zone and the drying zone. When the temperatures exceed or fall below a predetermined, and adjustable, limiting temperature, the preheating (or pre-cooling) is wholly or partially cut ofi by the impulses derived from the said thermal impulse emitters. These regulating impulses may also be used to cut oil or reduce the radiation supplied for drying purposes, for example by shutting off or throttling the supply offuel or by switching oil electric heating coils or infrared lamps.
  • a number of thermal impulse emitters may be arranged across the width of the belt. Each of these emitters affects only the longitudinal strip of the belt on which it is mounted, i. e. only cuts 05 or reduces'that portion of the pre-heating or pre-cooling means, and if desired of the drying radiation, which is arranged above the said longitudinal strip.
  • a belt drier for carrying out the process ofthe present invention must have a pre-treatment zone, in which the; heating or cooling means for the material are arranged, in advance of the drying zone and also have one or more thermal impulse emitters arranged between the two zones, which may simultaneously control the heating or cooling means of the two zones.
  • the invention also provides an apparatus for the drying by radiation of moist material spread on a drying belt, which comprises means for p're-heating or, pre-cooling the material on the belt, one or more thermal impulse emitters, adjustable to a desired limiting temperature, arranged above the belt, and one or more radiation heaters for drying the material, the said thermal impulse emitter or emitters controlling the amount of heat supplied to the material by the radiation heater or heaters and if desired also controlling the.
  • the thermal impulse emitters are mounted at such a distance from the drying radiation zone that their controlling impulses are received in sufficient time, allowing for the heat inertia of the heat-radiating elements, to bring the radiation energy to the correct value necessary to dry that part of the layer of moist material which is just entering the drying zone.
  • thermal impulse emitters and possibly also the pre-heating or pre-cooling zones, to be arranged so that they are movable longitudinally of the belt, so that they may be brought'closer to the drying zone when the belt velocity is smalland moved further away from the drying'zone when the belt velocity is high.
  • Figure l is a side elevation of a vacuum belt drier suitable for carrying out the method according to the invention and having a pre-heating zone in which the heating is effected by radiation,
  • Figure 2 is 'a plan view of the drier
  • Figure 3 is'a side elevation of'a belt drier in which the pre-heating or pre-cooling in the regulating zone is effected by blowing steam or air on to the moist material, and
  • Figure 4 is a plan view ofthe drier'illustrated in Figure '3.
  • moist material which is to be driedis spread by means of a distributor means 4 on a drying belt 1, which travels over rollers 2'and 3 in the direction of the arrow.
  • the temperature of this layer of moist material is determined by means .of thermometers 5, which are slidingly arranged on the belt 1 and are protected by a radiation screen 6.
  • the material then passes through a pre-heating zone which is formed by electric heat-radiating elements 7.
  • thermometers 5 may be, allowed for either manually or automatically.
  • Thermal impulse emitters in the form of contact thermometers 8 are slidably arranged on the belt at the end of the pre-heating zone.
  • the limiting temperature is adjustable; if this temperature is exceeded a circuit 9 is briefly closed or opened so that the irradiation of the heating element 7 is reduced and at the same time an electromagnetically operated valve 10 is closed and interrupts the supply of fuel to the drying zone.
  • the heating of the drying zone is effected by radiation tubes '11, which are heated by means of gas flames 12.
  • the pre-heating coil 7 is switched on again and at the same time the electromagnetic valve 10 is lifted, so that gas again flows and, after being ignited by a pilot light 13, heats the radiation tubes 11.
  • the combustion gases are exhausted through an ejector 14.
  • the dried material falls down at the rear reversing roller 3, and may then be finally treated in a further drying device.
  • the temperature at this point here determined by a thermometer which is protected against radiation, serves to indicate the residual moisture content of the material at the end of the radiation drying zone. According to the value which is measured here, the limit contacts of the contact thermometer 8 may be adjusted manually or automatically.
  • a discharge pipe 19 is provided for withdrawing gases from a vacuum chamber 16.
  • the pipe 19 is connected to a vacuum pump (not shown).
  • the outside air pressure forces the moist ma terial from a container 17 by way of the pipe 4 to one end of the belt 1.
  • the dried material drops from the other end of the belt into a container 18, from which it is removed at intervals.
  • the drier shown in Figures 3 and 4 differs from that shown in Figures 1 and 2 in that the radiation heating element 7 ( Figures 1 and 2), in the zone following the radiation screen 6, is replaced by discharge openings 20 from which vapours for heating the material spread on 4. the belt 1 or air for cooling the said material may be discharged as required.
  • the vapours or the air pass from a main pipe 21 to discharge openings 20 by Way of pipes 22.
  • Electric heating elements 23 are provided as radiators for the drying zone in the form of apparatus shown in Figures 3 and 4, instead of the radiation tubes 11 provided in the apparatus shown in Figures 1 and 2.
  • the vapour or air blown on to the material raises or lowers the temperature of the moist material spread out on the belt; the resulting variation in temperature depends either on the heat capacity of the moist material, if the blowing action is kept constant over a period of time, or, as in the form of apparatus shown, is so controlled that it experiences relatively large or small fluctuations about a constant value. Variations in the temperatures of admission at the thermometers 5 may be allowed for manually or automatically. Thermal impulse emitters in the form of contact thermometers 8 are slidably arranged on the belt between the pre-heating or pre-cooling zone and the drying zone.
  • the limit temperature is adjustable; if this temperature is exceeded the circuit 9 is short-circuited or otherwise interrupted so that the radiation of the electrical heating elements 23 is reduced and at the same time the valve10 is closed.
  • This valve is here shown electromagnetically actuated by means of a magnet winding 24.
  • the closing of the valve 10 causes the supply of vapour or air from the main pipe 21 to the discharge openings or nozzles 20 to be shut off.
  • the temperature registered by the contact thermometer 8 drops again the radiation heating system 23, and the supply of vapour or air through the nozzles 20, are switched on again.
  • thermal contact indicates both physical contact and heat or thermal contact which is not-physical contact.
  • Method for drying moist material which comprises substantially continuously passing a layer of moist material through a regulation zone and thereafter passing said material through a drying zone, subjecting said material to radiant heat in said drying zone to dry the same; subjecting the material to a predetermined caloric change in said regulation zone determining the temperature differential caused by said caloric change and varying the amount of radiant heat supplied in said drying zone in proportion to said temperature differential occurring in said regulation zone.
  • Method according to claim 1 which includes varying said predetermined caloric change and said radiant heat supply to said drying zone in accordance with the temperature of the material located between said zones.
  • a radiant heat drier for drying moist material having means for passing moist material to and through a drying zone containing a radiant heater; a regulation zone positioned for passage of a layer of moist material therethrough prior to passage into said drying zone, heat exchange means positioned in said regulation zone for imparting a caloric change to the material passing therethrough, temperature sensitive means responsive to temperature differential imparted to the'moist material by said heat exchange means, and means actuated by said temperature sensitive means for varying the heat output of said radiant heater in proportion to said temperature differential.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
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  • Drying Of Solid Materials (AREA)

Description

Feb. 24, 1959 A. HALTMEIER 2,874,482
DRYING OF MOIST MATERIAL Filed Aug. 9. 1954 2 Sheds-Sheet 1 FIG] IN VEN TOR. A LFRED H L TMEIER v "W M ATTORNEYS Feb. 24, 1959 A HALTMEIER 2,874,482
' DRYINGOF MOIST MATERIAL I 2 Sheets-Sheet 2 Filed Aug. 9. 1954 FIG. 4
INVENTOR. ALFRED HALTMEIE R A T TURNEYS United States Patent "ice DRYING or MOIST MATERIAL Alfred Haltmeier, Leverkusen-Bayerwerk, Germany, as-
signor to Farbenfabriken Bayer Aktiengesellschaft, Leverkusen, Germany, a corporation of Germany Application August 9, 1954, Serial No. 448,683
The present invention relates to an improved method of, and apparatus for, drying material on a belt drier by radiation. A
When material on a belt drier is to be dried by radiatio it is essential to adapt the amount of radiation to the amount of moisture to be removed from the material. If the amount of radiated energy absorbed is greater than the sum of the latent and sensible heat capacity of the moist material, the material being dried becomes overheated and, if the said material is sensitive to temperature, valuable properties may by deleteriously affected.
An indication of the amount of moisture still remaining in the material being dried is given by the temperature of the material at the end of the radiation drying zone;
this temperature may, for example, be determined by means of thermometers, protected against the radiation, which contact the belt at this position. The more this final temperature exceeds the temperature at which the moisture evaporates from the material being dried,-the less is the amount of moisture remaining; it'is thus possible to take advantage of the temperatures of the dried material at the end of the radiation zone for regulating the amount of residual moisture in the undried material. If the material is dried under reducedpressur'e, the temperature at which the moisture evaporates depends on the pressure used.
It is unfortunate, however, that the regulating impulses which can be obtained by making use of the variations in temperature of the material undergoing drying usually come too late, as materials which are sensitive to temperature may already have been damaged before they have reached the end of the radiation zone.
In accordance with the present invention it has now been found that variations in the temperature of the moist material spread on the belt, before the material enters the radiation drying zone,can be utilised for regulating the amount of radiated heat supplied. Accordingly the:
present invention provides a method ofdrying moist material by spreading the moist material on the belt of a belt drier and drying the material by radiation, wherein .the moist material on the belt is pre-heated or pre-cooled and the resulting variations in temperature of the material are used to control the amount of radiated heat supplied to the material to dry it. This preheating and/ or precooling of the moist material is referred to in the claims as' thermally varying the temperature of the moist material. These variations in the temperature of the moist material spread on the belt may be obtained either by heating by preliminary irradiation or by a current of vapour being blown thereon, or by cooling by blowing on air.
The amount of radiated-heat supplied may be controlled by the variations in temperature of the heated or cooled material in various ways. If the rate at which radiated heat is supplied to the moist material is kept constant for a time, the material is heated more as its heat capacity 2,874,482 Patented Feb. 24, 1959 moist material is spread. If the rate of Preliminary heating or preliminary cooling is kept constant for a time, the rise or fall thus produced in the temperature of the material on the belt may be used to control the rate at which radiation energy is supplied to the drying zone, for ex-' ample by using electrical or perhaps pneumatic transmission devices to supply to the radiation heaters an amount of fuel or electric power which is proportional to the rise or fall in the temperature of the moist material resulting from the pre-heating or pre-cooling.
This result may be simply obtained if the pre-heating or pre-cooling is so regulated that the rate of rise-or fall in the temperature of the moist material spread on the belt remains constant over a period of time. Controlling impulses may be supplied by temperature governors or difierential governors; these impulses may then be used simultaneously to regulate the pre-heating or pro-cooling of the material and to control the radiation to be subsequently used for drying purposes. Owing to the high thermal inertia of heating systems operated with gas, oil or elec tricity, it is possible to operate with simple limiting contact regulators. a
Thermal impulse emitters such as thermo-elements, resistanee thermometers or contact thermometers, arranged to slideon the, belt. or total radiation pyrometers if the layer of material is not to be damaged, are arranged between the pro-heating or pre-cooling zone and the drying zone. When the temperatures exceed or fall below a predetermined, and adjustable, limiting temperature, the preheating (or pre-cooling) is wholly or partially cut ofi by the impulses derived from the said thermal impulse emitters. These regulating impulses may also be used to cut oil or reduce the radiation supplied for drying purposes, for example by shutting off or throttling the supply offuel or by switching oil electric heating coils or infrared lamps.
In order to allow for local fluctuations in the thickness of the layer of the moist material, such as are caused by the distributing slot which feeds the moist material on to the belt becoming clogged at one side, a number of thermal impulse emitters may be arranged across the width of the belt. Each of these emitters affects only the longitudinal strip of the belt on which it is mounted, i. e. only cuts 05 or reduces'that portion of the pre-heating or pre-cooling means, and if desired of the drying radiation, which is arranged above the said longitudinal strip.
A belt drier for carrying out the process ofthe present invention must have a pre-treatment zone, in which the; heating or cooling means for the material are arranged, in advance of the drying zone and also have one or more thermal impulse emitters arranged between the two zones, which may simultaneously control the heating or cooling means of the two zones. Accordingly, 'the invention also provides an apparatus for the drying by radiation of moist material spread on a drying belt, which comprises means for p're-heating or, pre-cooling the material on the belt, one or more thermal impulse emitters, adjustable to a desired limiting temperature, arranged above the belt, and one or more radiation heaters for drying the material, the said thermal impulse emitter or emitters controlling the amount of heat supplied to the material by the radiation heater or heaters and if desired also controlling the.
amount of pre-heating or pre-cooling. The thermal impulse emitters are mounted at such a distance from the drying radiation zone that their controlling impulses are received in sufficient time, allowing for the heat inertia of the heat-radiating elements, to bring the radiation energy to the correct value necessary to dry that part of the layer of moist material which is just entering the drying zone. With a belt travelling at a relatively high speed,
this distance must be greater than when the belt is travela) ling more'slowly. Consequently, it is advisable for the thermal impulse emitters, and possibly also the pre-heating or pre-cooling zones, to be arranged so that they are movable longitudinally of the belt, so that they may be brought'closer to the drying zone when the belt velocity is smalland moved further away from the drying'zone when the belt velocity is high.
In the accompanying diagrammatic drawings:
Figure l is a side elevation of a vacuum belt drier suitable for carrying out the method according to the invention and having a pre-heating zone in which the heating is effected by radiation,
Figure 2 is 'a plan view of the drier,
Figure 3 is'a side elevation of'a belt drier in which the pre-heating or pre-cooling in the regulating zone is effected by blowing steam or air on to the moist material, and
Figure 4 is a plan view ofthe drier'illustrated in Figure '3.
Referring to Figure 1, moist material which is to be driedis spread by means of a distributor means 4 on a drying belt 1, which travels over rollers 2'and 3 in the direction of the arrow. The temperature of this layer of moist material is determined by means .of thermometers 5, which are slidingly arranged on the belt 1 and are protected by a radiation screen 6. The material then passes through a pre-heating zone which is formed by electric heat-radiating elements 7. Asa result of the initial r'adiation the temperature of the moist material spread on the belt rises; this rise in temperature depends on the heat capacity of the moist material if the amount of-radiation is kept constant or, as assumed in the drawing, is so controlled that it'undergoesirelatively large or small fluctuations on either side of a constant value. Variations in the temperature of the material entering the pretreatment zone at the thermometers 5 may be, allowed for either manually or automatically. Thermal impulse emitters in the form of contact thermometers 8 are slidably arranged on the belt at the end of the pre-heating zone. The limiting temperature is adjustable; if this temperature is exceeded a circuit 9 is briefly closed or opened so that the irradiation of the heating element 7 is reduced and at the same time an electromagnetically operated valve 10 is closed and interrupts the supply of fuel to the drying zone. In the form of apparatus shown in the figure the heating of the drying zone is effected by radiation tubes '11, which are heated by means of gas flames 12.
When the temperature registered by the contact thermometer 8 drops again, the pre-heating coil 7 is switched on again and at the same time the electromagnetic valve 10 is lifted, so that gas again flows and, after being ignited by a pilot light 13, heats the radiation tubes 11. The combustion gases are exhausted through an ejector 14. The dried material falls down at the rear reversing roller 3, and may then be finally treated in a further drying device. The temperature at this point, here determined by a thermometer which is protected against radiation, serves to indicate the residual moisture content of the material at the end of the radiation drying zone. According to the value which is measured here, the limit contacts of the contact thermometer 8 may be adjusted manually or automatically. A discharge pipe 19 is provided for withdrawing gases from a vacuum chamber 16. The pipe 19 is connected to a vacuum pump (not shown). The outside air pressure forces the moist ma terial from a container 17 by way of the pipe 4 to one end of the belt 1. The dried material drops from the other end of the belt into a container 18, from which it is removed at intervals.
The drier shown in Figures 3 and 4 differs from that shown in Figures 1 and 2 in that the radiation heating element 7 (Figures 1 and 2), in the zone following the radiation screen 6, is replaced by discharge openings 20 from which vapours for heating the material spread on 4. the belt 1 or air for cooling the said material may be discharged as required. The vapours or the air pass from a main pipe 21 to discharge openings 20 by Way of pipes 22. Electric heating elements 23 are provided as radiators for the drying zone in the form of apparatus shown in Figures 3 and 4, instead of the radiation tubes 11 provided in the apparatus shown in Figures 1 and 2.
The vapour or air blown on to the material raises or lowers the temperature of the moist material spread out on the belt; the resulting variation in temperature depends either on the heat capacity of the moist material, if the blowing action is kept constant over a period of time, or, as in the form of apparatus shown, is so controlled that it experiences relatively large or small fluctuations about a constant value. Variations in the temperatures of admission at the thermometers 5 may be allowed for manually or automatically. Thermal impulse emitters in the form of contact thermometers 8 are slidably arranged on the belt between the pre-heating or pre-cooling zone and the drying zone. The limit temperature is adjustable; if this temperature is exceeded the circuit 9 is short-circuited or otherwise interrupted so that the radiation of the electrical heating elements 23 is reduced and at the same time the valve10 is closed. This valve is here shown electromagnetically actuated by means of a magnet winding 24. The closing of the valve 10 causes the supply of vapour or air from the main pipe 21 to the discharge openings or nozzles 20 to be shut off. When the temperature registered by the contact thermometer 8 drops again the radiation heating system 23, and the supply of vapour or air through the nozzles 20, are switched on again.
I The term, thermal contact, as used in the claims, indicates both physical contact and heat or thermal contact which is not-physical contact.
I claim:
1. Method for drying moist material which comprises substantially continuously passing a layer of moist material through a regulation zone and thereafter passing said material through a drying zone, subjecting said material to radiant heat in said drying zone to dry the same; subjecting the material to a predetermined caloric change in said regulation zone determining the temperature differential caused by said caloric change and varying the amount of radiant heat supplied in said drying zone in proportion to said temperature differential occurring in said regulation zone.
2. Method according to claim 1 in which caloric change is effected by heat radiation.
3. Method according to claim 1 in which caloric change is effected by blowing heating vapors thereon.
4. Method according to claim 1 in which caloric change is effected by blowing cooling gas thereon.
5. Method according to claim 1 which includes varying said predetermined caloric change and said radiant heat supply to said drying zone in accordance with the temperature of the material located between said zones.
6. Method according to claim 1 in which said caloric change and said radiant heat supply to said drying zone are simultaneously varied in accordance with the temperature of the material located between said zones.
7. In combination with a radiant heat drier for drying moist material having means for passing moist material to and through a drying zone containing a radiant heater; a regulation zone positioned for passage of a layer of moist material therethrough prior to passage into said drying zone, heat exchange means positioned in said regulation zone for imparting a caloric change to the material passing therethrough, temperature sensitive means responsive to temperature differential imparted to the'moist material by said heat exchange means, and means actuated by said temperature sensitive means for varying the heat output of said radiant heater in proportion to said temperature differential.
8. Combination in accordance with claim 7 including References Cited in the file of this patent UNITED STATES PATENTS 10 Harvey Sept. 16, 1924 6. Field Apr. 13, 1926 Staege May 29, 1928 Olsen May 23, 1944 Ross et a1. Dec. 18, 1945 New May 13, 1947 Meienhofer Apr. 13, 1954 Haltmeier Mar. 29, 1955
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Cited By (12)

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US3204341A (en) * 1961-11-27 1965-09-07 Ashland Oil Inc Process and apparatus for drying wet particulate material to a desired moisture content
US3214845A (en) * 1961-05-24 1965-11-02 Industrial Nucleonics Corp Moisture measuring and selective dryer control system
US3259995A (en) * 1964-02-03 1966-07-12 Proctor & Schwartz Inc Moving material drying method and apparatus
US3266558A (en) * 1962-07-30 1966-08-16 Griffon Henri Apparatus for dehydration of pasty substances
US3367038A (en) * 1965-03-18 1968-02-06 Copolymer Rubber & Chem Corp Method and apparatus for moisture detection, monitoring and control in drying materials
US3525163A (en) * 1968-11-29 1970-08-25 Armstrong Cork Co Method of drying nodular fiberboard
US3791049A (en) * 1971-10-04 1974-02-12 Smitherm Industries Drying methods with moisture profile control
US3851403A (en) * 1972-04-19 1974-12-03 Agfa Gevaert Ag Apparatus for conditioning sheets of photosensitive materials
US4774831A (en) * 1985-01-25 1988-10-04 Ulf Nordin Method and a device for determining moisture content
US6401358B1 (en) * 1998-02-23 2002-06-11 Advanced Photonics Technologies Ag Method and device for drying a rapidly conveyed product to be dried, especially for drying printing ink
EP1302736A2 (en) * 2001-10-16 2003-04-16 J.A. Niemeijer B.V. System for thickening and drying manure
FR2875721A1 (en) * 2004-09-28 2006-03-31 Sita Fd Sa Drying concentrates obtained by evaporation of landfill leachates comprises use of scraper conveyor with crust-breaking projections and biogas-fired infrared radiants

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US1508516A (en) * 1923-12-13 1924-09-16 Arthur R Harvey Instrument for the automatic determination of moisture in paper or textiles
US1580658A (en) * 1921-01-05 1926-04-13 Field Crosby Drying apparatus
US1671493A (en) * 1925-05-04 1928-05-29 Westinghouse Electric & Mfg Co Dryness controller
US2349300A (en) * 1942-01-02 1944-05-23 Western Cartridge Co Explosive
US2391195A (en) * 1943-03-16 1945-12-18 J O Ross Engineering Corp Drier
US2420399A (en) * 1941-06-12 1947-05-13 Francis H M New Thread drier having radiant heaters and automatic control means
US2674809A (en) * 1950-08-24 1954-04-13 Raduner & Co Ag Apparatus for thermic treatment by infrared radiation
US2705137A (en) * 1949-12-16 1955-03-29 Bayer Ag Belt drier heated by radiation

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US1580658A (en) * 1921-01-05 1926-04-13 Field Crosby Drying apparatus
US1508516A (en) * 1923-12-13 1924-09-16 Arthur R Harvey Instrument for the automatic determination of moisture in paper or textiles
US1671493A (en) * 1925-05-04 1928-05-29 Westinghouse Electric & Mfg Co Dryness controller
US2420399A (en) * 1941-06-12 1947-05-13 Francis H M New Thread drier having radiant heaters and automatic control means
US2349300A (en) * 1942-01-02 1944-05-23 Western Cartridge Co Explosive
US2391195A (en) * 1943-03-16 1945-12-18 J O Ross Engineering Corp Drier
US2705137A (en) * 1949-12-16 1955-03-29 Bayer Ag Belt drier heated by radiation
US2674809A (en) * 1950-08-24 1954-04-13 Raduner & Co Ag Apparatus for thermic treatment by infrared radiation

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3214845A (en) * 1961-05-24 1965-11-02 Industrial Nucleonics Corp Moisture measuring and selective dryer control system
US3204341A (en) * 1961-11-27 1965-09-07 Ashland Oil Inc Process and apparatus for drying wet particulate material to a desired moisture content
US3266558A (en) * 1962-07-30 1966-08-16 Griffon Henri Apparatus for dehydration of pasty substances
US3259995A (en) * 1964-02-03 1966-07-12 Proctor & Schwartz Inc Moving material drying method and apparatus
US3367038A (en) * 1965-03-18 1968-02-06 Copolymer Rubber & Chem Corp Method and apparatus for moisture detection, monitoring and control in drying materials
US3525163A (en) * 1968-11-29 1970-08-25 Armstrong Cork Co Method of drying nodular fiberboard
US3791049A (en) * 1971-10-04 1974-02-12 Smitherm Industries Drying methods with moisture profile control
US3851403A (en) * 1972-04-19 1974-12-03 Agfa Gevaert Ag Apparatus for conditioning sheets of photosensitive materials
US4774831A (en) * 1985-01-25 1988-10-04 Ulf Nordin Method and a device for determining moisture content
US6401358B1 (en) * 1998-02-23 2002-06-11 Advanced Photonics Technologies Ag Method and device for drying a rapidly conveyed product to be dried, especially for drying printing ink
EP1302736A2 (en) * 2001-10-16 2003-04-16 J.A. Niemeijer B.V. System for thickening and drying manure
EP1302736A3 (en) * 2001-10-16 2007-05-09 J.A. Niemeijer B.V. System for thickening and drying manure
FR2875721A1 (en) * 2004-09-28 2006-03-31 Sita Fd Sa Drying concentrates obtained by evaporation of landfill leachates comprises use of scraper conveyor with crust-breaking projections and biogas-fired infrared radiants

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