US2290350A - Atomizing system - Google Patents

Atomizing system Download PDF

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US2290350A
US2290350A US295400A US29540039A US2290350A US 2290350 A US2290350 A US 2290350A US 295400 A US295400 A US 295400A US 29540039 A US29540039 A US 29540039A US 2290350 A US2290350 A US 2290350A
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pump
pressure
oil
atomizer
return
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US295400A
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Albert P Olches
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Peabody Engineering Corp
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Peabody Engineering Corp
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D11/00Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space
    • F23D11/24Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space by pressurisation of the fuel before a nozzle through which it is sprayed by a substantial pressure reduction into a space
    • F23D11/26Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space by pressurisation of the fuel before a nozzle through which it is sprayed by a substantial pressure reduction into a space with provision for varying the rate at which the fuel is sprayed
    • F23D11/28Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space by pressurisation of the fuel before a nozzle through which it is sprayed by a substantial pressure reduction into a space with provision for varying the rate at which the fuel is sprayed with flow-back of fuel at the burner, e.g. using by-pass

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  • This invention relates to atomizer systems utilizing a mechanical atomizer which is ccntrolled by withdrawing a controlled portion of the fluid from the atomizer tip through a fluid return line.
  • a mechanical atomizer which is ccntrolled by withdrawing a controlled portion of the fluid from the atomizer tip through a fluid return line.
  • the invention is described herein as applied to a fuel oil burning system but it should be understood that the invention is not to be limited thereto but may be applied toA various uses.
  • the Graham et al. Patent 1,824,952 shows a system of this general type utilizing a mechanical atomizer having a tip in which the oil is delivered under pressure to a central whirling chamber through tangential passages which imparta rapid whirling motion to the oil whereby it is discharged from the tip oriilce in the form of a cone-shaped spray.
  • the operating capacity of the atomizer is varied over a-wide range by withdrawing from the whirling chamber a centrolled portion of the oil from the atomizer tip through an oil return line.
  • the total quantity of oil pumped to the atomizer equals the quantity sprayed lplus the quantity returned, all of which passes through the tangentialpassages.
  • the total quantity is dependent upon the pressure drop across the tangential passages.
  • Both the quantity and pressure drop may be maintained substantially constant by regulating the oil supply pressure in accordance with the variations in pressure in the return line or vice versa as more fully disclosed in the Graham et a1. patent, above mentioned.
  • the speed of rotation in the atomizer hence the neness of atomization, are maintained substantially constant throughout a wide operating eapacity range.
  • the above described atomizer is referred to herein, for convenience, as an atomizer of the variable return type.
  • Another object is to provide an oil burning system of the type above indicated having novel and improved means for automatically maintaining a substantially constant pressure difierential between the inlet and return lines or across the atomizer tip.
  • Another object is to provide an oil burning system of the type above indicated, having novel and improved means for automatically regulating the quantity of oil pumped to an atcmizer system.
  • Another object is to provide s'uch a system in which the hot return oil is always maintained 55 (c1. 29o-5e) under positive pressure so that vapor locks or the like are eliminated.
  • Another object is to provide a system of the above type having improved operating characteristics.
  • a further object is to provide such a system which is simple and dependable in operation and requires'a minimum of equipment.
  • Another object is to provide a system of the above type which is adapted to commercial oil burner operatio
  • Various other objects and advantages will be apparent as the nature of the invention is 'more rully disclosed.
  • Fig. 1 is a diagrammatic view illustrating an oil burning system embodying the present invention
  • Fig. 2 is a diagrammatic view similar to Fig. 1 showing a different embodiment of the invention
  • Figs. 3 and 4 are series of curves representingr the operating characteristics of the system.
  • Fig. 1 the invention is shown in Fig. 1 as applied to a system for supplying oil to a plurality of atomizers 9 of the general type described in the Graham et al. patent above mentioned.
  • the oil is supplied by a line I0 to the suction side of a pump Il which is capable of raising the oil to a pressure in excess of any pressure at which it may be desired to operate the return line to be described.
  • the oil is then passed through a heater I2 of any suitable construction by which its temperature may be raised so as tc facilitate the operation of the atomizer.
  • the pump Il and the heater I2 comprise conventional auxiliary equipment ,for a fuel oil burning installation. Hence, the present invention may easily be addedto existing pumping and heating sets.
  • the oil passes through a line M, its flow being regulated by a control valve l5, to the suction side of a pump I6, reierred to herein for convenience as .a hot oil pump.
  • Thecontrol valve II regulates the quantity of oil in accordance with the atomizer re- ⁇ opening of the Valve.
  • the oil passes through a supply line the high pressure side andsthe low pressure side of the hot oil pump I6 by means of lines 2
  • This relief valve may be used for excess pressure protection or maybe set to maintain a constant pressure differential across the pump I6.
  • a manually controlled by-pass valve 23 may also be connected in parallel with relief valve 20 between the high and low pressure sides of the pump I6 for regulating the pump capacity as will be described.
  • the atomizers and the hot oil pump constitute a closed system continually circulating oil.
  • the atomizers continually spray oil into the furnace, thus removing a portion thereof from the circulating system, it is necessary to continuously make up .this portion by supplying the same to the system from an outside source.
  • th'e quantity of oil pumped to the atomizers by the hot oil pump (Qc) is equal to the sum of the quantity of oil returned from the atomizers (Q2) and the quantity of oil sprayed by the atomizers (Q3).
  • 'I'he pressure P3 in the return line I8 and on the lowvpressure side of the pump I6 is controlled by the valve I5.
  • 'I'he pressure Pu in the line II is determined by the pressure P3 and by the operating characteristics of the pump I6.
  • the relief valve 20 may be adjusted to maintain a given pressure differential Po-P: regardless of variations in load. Under these conditions, if the load is varied, as for example by cutting one or more atomizers out of service, the same pressure differential would be maintained and the atomizers still in service would continue to operate at the same individual capacities. This is an important feature in oil burning installations wh'ere the air supply must be adjusted in accordance with the individual atomizer capacity to effect eilicient combustion and any change in individual atomizer capacity would require readjustment of the air supply.
  • the pump I6 may be of any commercial form but preferably is of the rotary type in order to avoid uctuations in pressure such as would be obtained with a piston -type pump. If of the rotary type, it may be a centrifugal pump or any type of positive displacement pump, such as a screw pump or a gear pump.
  • the pump I 6 is a positive displacement pump operated at constant speed
  • the system will operate as above described with the relief valve 20 in service.
  • the hot oil pump is of a positive displacement type and is so designed as to deliver exactly the maximum capacity required by the system
  • relief valve 20 is set at a slightly higher pressure than the maximum produced by the pump when delivering the maximum quantity
  • the pump will deliver a constant volume regardless of the pressure Ps at the intake side of the pump,and the quantity of oil.
  • pumped Q0 will be in accordance with curve 38 in Fig. 4, even though there is friction in the lines connecting the pump to the atomizers.
  • the positive displacement hot oil pump I6 will then be designed to supply a quantity of oil in excess of the maximum quantity required to be pumped to the burners and Qu may be regulated by adjustment of the valve 23 which permits the excess oil to be by-passed to the low pressure side of the pump.
  • relief valve 20 may be set at a. suiliciently high pressure so that it will not operate during actual service and will merely serve as a pressure protection in case the system should become disturbed, as by the closing of a, valve and the pressure Po should rise to a value to endanger the pump casing.
  • the system would then also operate in a manner above described and in accordance with the curves 38 and 39 of Fig. 4, the valve 23, however, permitting adjustments to be made to adapt the system to the required operating conditions.
  • the relief valve may be set to operate in response to a limited pressure rise above the normal operatinghpressure. If the pressure should then rise, due, for example, to cutting out an atomizer, to the point at which the relief valve 20 is set to operate, the valve would serve to maintain this constant pressure across the pump and the system would operate as a constant differential system as represented by the curve 40 of Fig. 4 until the pressure again falls below the above mentioned point.
  • the burner When thus operating in the straight mechanical' range, that is above point 28 in Fig. 3, the burner may have the characteristics represented by the curve 21 in Fig. 3. When the pressure on the Fig. 3.
  • the relief valve 20 may of course be connectedacross the lines I1 and I8 at or near the atomizers, if desired, so as to eliminate from consideration any variations in pressure in the lines themselves.
  • the connection of the relief valve between points near the atomizer will cause the curve 25 or 4U, representing the oil pumped to be more nearly horizontal, approaching curve 38 of Fig. 3.
  • Connection of the valve at a point directly across the hot oil pump causes the operating curve 25 of Fig. 3 or 40 of Fig. 4 to be inclined due principally to the variation in pressure drop in the return line as the diierent quantities oi oil are withdrawn therethrough.
  • the hot oil pump 36 is of the type delivering a constant head regardless of the quantity.
  • a valve 31 is shown as connected between the high Pressure Side 0f the hot oil pump 36 and the supply line I1. This valve constitutes, in effect, an adjustable xed orifice which reduces the 'pressure in the line I1.
  • the purpose of the valve is to permit the system to be adjusted to maintain a given pressure differential between the supply and return lines without varying the hot oil pump itself should it not deliver the exact head required.
  • the hot oil pump 3B will be designed to maintain a pressure diierential greater than that desired between the supply and return lines.
  • the pressure in the supply line is then reduced by means of the adjustable fixed oriice valve 31 so that the total pressure across the pump and the valve 31 becomes equal to that which it is desired to maintain between the supply and return lines.
  • the system will then operate in accordance with the curves of Figs. 3 and 4 as above described.
  • the above described systems are simple to operate and require a minimum amount of equipment. They are adapted to the operation of single atomizers or'of a plurality of atomizers in parallel.
  • the pump II may be omitted.
  • the preheater I2 may likewise be omitted, if desired, without changing the operation of the present system.
  • the pump II maintains a positive pressure on the low pressure side of the pump I6 and in the return line I8. Hence, the hot oil is maintained under'a head at all times and the tendency for a vapor lock to Iormband interfere with the operation of the system is avoided.
  • a fluid atomizing system comprising an atomizer of the variable return type having a tip provided with a whirling chamber in which a rotary movement is imparted to the fluid and having an Arthur from which part of the rotating fluid is discharged for atomization, a supply conduit connected to suply fluid to said whirling chamber, a return conduit connected to withdraw a portion of the rotating fluid from said whirling chamber, constant pressure differential pump means connected to receive iiuid from said return conduit and to discharge said fluid to said supply conduit at a predetermined constant increase in pressure to thereby maintain a constant pressure differential between said supply and return conduits, a feed conduit connected to supply to said return conduit fluid to be atommized and to control the iluid pressure in said return conduit, and means to control the fiuid pressure in said feed conduit to thereby vary the capacity of said atomizer while maintaining by means of said pump means a. predetermined pressure differential between said supply'and return conduits.
  • a control valve connected between the high and low pressure sides olf said pump, said valve maintaining a. substantially constant pressure diierentialtherebetween.
  • a fluid atomizing system as set forth in claim 1 in which a pump is included in said feed conduit to maintain a positive pressure on the low pressure side of said constant pressure differential pump suited to avoid vapor lock and a. valve is provided in said feed line to control the pressure of the fluid supplied to said return line.
  • a check valve in said return conduit to prevent reverse flow of iluid therein to said atomlzer tip, whereby straight mechanical opera-- tion without uid return is obtained when the .pressure in said feed conduit is higher than the pressure in said tip.
  • variable return atomizer of the type having an atomizing tip provided with a whirling chamber in which a rotary movement is imparted to the iiuid and having an orifice from which part of the rotating fluid is discharged for atomization and having a fluid supply conduit to and a fluid return conduit Ifrom said whirling chamber and constant .
  • pressure diierential pump means connected therebetween to recirculate the returned fluid, which method comprises supplying the fiuid from a source to the low pressure side of said pump and varying the atomizer capacity by controlling the pressure of said source while maintaining, by means of said pump means, a constant pressure differential between the su-pply and return conduits.
  • the method of controlling the burner output of a mechanically atomizing oil burner forming .part od a closed oil circulating system including the said burner, a pump for pumping oil to said burner, an oil supply line from said pump to saidl burner and an oil return line from said burner to said pump, comprising, utilizing a constant volume pump having a capacity greater than that required, by-passing around said pump a predetermined portion of the oil pumped, supplying to the said burners the constant volume of oil not lay-passed, returning excess oil not burned through an unrestricted return line, supplying oil to said system to make u-p the quantity of oil burned, and controlling the quantity of oil burned by regulating the quantity of make-.up oil supplied.
  • Method of coroning the liquid sprayed .by a mechanical atomizer of the type wherein liquid is supplied to the atomizer tip at a ilow in excess of that at which said liquid is atomized which comprises. establishing a constant volume flow from a pump to said atomizer at a value in excess of that at which liquid is atomized by said atomizer, recirculating excess ilow backl to said pump in a closed circulating system, supplying make-up liquid from a source of liquid to said circulating system, and controlling the quantity of liquid atomized by regulating the flow of make-up liquid to said circulating system at a point intermediate said source and said circulating system.

Description

July 21, 1942. A. P. oLcHEs ATOMIZINYCTv SYSTEM v Filed Sept. 1s. 1939 da l PUMP
Z3) RELIEF VALVE ou. PuMPEo M0) HEATE R INVENTOR leri UIC/Ms BY I l l/ TORNEY Patented July 21, 1942 ATOMIZING SYSTEM Albert P. Olches, West Hempstead, Long Island,
N. Y., ration, New York, N. Y., York assignor to Peabody Engineering Corpoa corporation of New Application September 18, 1939, ISerial No. 295,400
Claims.
This invention relates to atomizer systems utilizing a mechanical atomizer which is ccntrolled by withdrawing a controlled portion of the fluid from the atomizer tip through a fluid return line. For convenience, the invention is described herein as applied to a fuel oil burning system but it should be understood that the invention is not to be limited thereto but may be applied toA various uses.
l The Graham et al. Patent 1,824,952 shows a system of this general type utilizing a mechanical atomizer having a tip in which the oil is delivered under pressure to a central whirling chamber through tangential passages which imparta rapid whirling motion to the oil whereby it is discharged from the tip oriilce in the form of a cone-shaped spray. The operating capacity of the atomizer is varied over a-wide range by withdrawing from the whirling chamber a centrolled portion of the oil from the atomizer tip through an oil return line. The total quantity of oil pumped to the atomizer equals the quantity sprayed lplus the quantity returned, all of which passes through the tangentialpassages. Hence, the total quantity is dependent upon the pressure drop across the tangential passages. Both the quantity and pressure drop may be maintained substantially constant by regulating the oil supply pressure in accordance with the variations in pressure in the return line or vice versa as more fully disclosed in the Graham et a1. patent, above mentioned. In this manner the speed of rotation in the atomizer, hence the neness of atomization, are maintained substantially constant throughout a wide operating eapacity range. The above described atomizer is referred to herein, for convenience, as an atomizer of the variable return type.
It is an object of the presentv invention to provide a novel'and improved system of the general type above indicated.
Another object is to provide an oil burning system of the type above indicated having novel and improved means for automatically maintaining a substantially constant pressure difierential between the inlet and return lines or across the atomizer tip.
Another object is to provide an oil burning system of the type above indicated, having novel and improved means for automatically regulating the quantity of oil pumped to an atcmizer system.
Another object is to provide s'uch a system in which the hot return oil is always maintained 55 (c1. 29o-5e) under positive pressure so that vapor locks or the like are eliminated.
Another object is to provide a system of the above type having improved operating characteristics.
A further object is to provide such a system which is simple and dependable in operation and requires'a minimum of equipment.
Another object is to provide a system of the above type which is adapted to commercial oil burner operatio Various other objects and advantages will be apparent as the nature of the invention is 'more rully disclosed.
Although the novel features which are believed to be characteristic of this invention are pointed out more particularly in the claims appended hereto, the invention itself may be better understood by referring to the following description, taken in connection with the accompanying drawing, in which certain specic embodiments thereof have been set forth for purposes of illustration;
In the drawing:
Fig. 1 is a diagrammatic view illustrating an oil burning system embodying the present invention;
Fig. 2 is a diagrammatic view similar to Fig. 1 showing a different embodiment of the invention;
Figs. 3 and 4 are series of curves representingr the operating characteristics of the system.
Referring to the drawing more in detail, the invention is shown in Fig. 1 as applied to a system for supplying oil to a plurality of atomizers 9 of the general type described in the Graham et al. patent above mentioned. The oil is supplied by a line I0 to the suction side of a pump Il which is capable of raising the oil to a pressure in excess of any pressure at which it may be desired to operate the return line to be described. The oil is then passed through a heater I2 of any suitable construction by which its temperature may be raised so as tc facilitate the operation of the atomizer. The pump Il and the heater I2 comprise conventional auxiliary equipment ,for a fuel oil burning installation. Hence, the present invention may easily be addedto existing pumping and heating sets.
From the heater I2 the oil passes through a line M, its flow being regulated by a control valve l5, to the suction side of a pump I6, reierred to herein for convenience as .a hot oil pump. Thecontrol valve II regulates the quantity of oil in accordance with the atomizer re- `opening of the Valve.
quirements and also regulates the pressure on the low pressure side of the pump I6 and in the return line. The pressure in the atomizer tip, which controlsthe quantity sprayed through the orifice, is dependent uponthe pressure in the return line.
From the high pressure side of the hot oill pump I6, the oil passes through a supply line the high pressure side andsthe low pressure side of the hot oil pump I6 by means of lines 2| and 22 respectively. This relief valve may be used for excess pressure protection or maybe set to maintain a constant pressure differential across the pump I6. A manually controlled by-pass valve 23 may also be connected in parallel with relief valve 20 between the high and low pressure sides of the pump I6 for regulating the pump capacity as will be described.
In the operation of the present system; the atomizers and the hot oil pump constitute a closed system continually circulating oil. However, due to the fact that the atomizers continually spray oil into the furnace, thus removing a portion thereof from the circulating system, it is necessary to continuously make up .this portion by supplying the same to the system from an outside source. It is thus obvious that th'e quantity of oil pumped to the atomizers by the hot oil pump (Qc) is equal to the sum of the quantity of oil returned from the atomizers (Q2) and the quantity of oil sprayed by the atomizers (Q3). 'I'he pressure P3 in the return line I8 and on the lowvpressure side of the pump I6 is controlled by the valve I5. 'I'he pressure Pu in the line II is determined by the pressure P3 and by the operating characteristics of the pump I6.
For purposes of explanation, the condition of no return through the line I8 may be considered (Q2-:0). This condition would occur if a valve in the line I8 were closed, or if such a valve were opened and the pressure P3 made equalto the pressure which existed in the central chamber of the atomizer tip prior to the Under these conditions, the entire quantity pumped is discharged at the atomizer tip (Qo=Q3) and the pressure drop across the tangential slots of the atomizer tip will equal the pressure differential across th'e pump (P-P3), disregarding the pressure drop in the line l1.
If now the pressure P3 is reduced, as by regulation of the valve I5, the pressure in the atomizer tip, which produces the flow Q3 will be reduced, Q3 will decrease, oil will flow in the return line I8 and the pressure Pu--Ps will be slightly greater than the actual diierential across the slots of the atomizer tip due to the pressure drop in the piping between the pump and the atomizers.
If the connecting conduits were frictionless, maintaining a constant differential Po-Ps across the pump would also maintain a constant pressure differential across the atomizer slots of an equal value, and as all ofthe oil pumped passes through these slots, the. quantity of oil pumped at all capacities would be constant as indicated by curve 88 in Fig. 4. However, in practice, the connecting lines are not frictionless. Hence, maintaining a constant pressure Po-Ps across the pump results in a slightly lesser differential across the atomizer tip slots at reduced capacities when more oil is returned and the quantity of oil pumped will be less at reduced atomizer capacities as indicated by the curve 48 in Fig. 4.
The relief valve 20 may be adjusted to maintain a given pressure differential Po-P: regardless of variations in load. Under these conditions, if the load is varied, as for example by cutting one or more atomizers out of service, the same pressure differential would be maintained and the atomizers still in service would continue to operate at the same individual capacities. This is an important feature in oil burning installations wh'ere the air supply must be adjusted in accordance with the individual atomizer capacity to effect eilicient combustion and any change in individual atomizer capacity would require readjustment of the air supply.
In the system above described, the pump I6 may be of any commercial form but preferably is of the rotary type in order to avoid uctuations in pressure such as would be obtained with a piston -type pump. If of the rotary type, it may be a centrifugal pump or any type of positive displacement pump, such as a screw pump or a gear pump.
If the pump I 6 is a positive displacement pump operated at constant speed, the system will operate as above described with the relief valve 20 in service. However, if the hot oil pump is of a positive displacement type and is so designed as to deliver exactly the maximum capacity required by the system, then if relief valve 20 is set at a slightly higher pressure than the maximum produced by the pump when delivering the maximum quantity, the pump will deliver a constant volume regardless of the pressure Ps at the intake side of the pump,and the quantity of oil. pumped Q0 will be in accordance with curve 38 in Fig. 4, even though there is friction in the lines connecting the pump to the atomizers. In actual practice it would rarely happen that the pump would exactly conform to the capacity requirements and consequently it is usually necessary to provide an adjusting means such as th'e by-pass valve 23. The positive displacement hot oil pump I6 will then be designed to supply a quantity of oil in excess of the maximum quantity required to be pumped to the burners and Qu may be regulated by adjustment of the valve 23 which permits the excess oil to be by-passed to the low pressure side of the pump. In such a case, relief valve 20 may be set at a. suiliciently high pressure so that it will not operate during actual service and will merely serve as a pressure protection in case the system should become disturbed, as by the closing of a, valve and the pressure Po should rise to a value to endanger the pump casing. The system would then also operate in a manner above described and in accordance with the curves 38 and 39 of Fig. 4, the valve 23, however, permitting adjustments to be made to adapt the system to the required operating conditions.
With the hot oil pump I6 of the constant displacement type and operating without control by the relief valve 20, it is obvious that if one or more atomizers were cut out of service, the remaining-atomizers would not operate at their same capacities unless some means were provided to compensatefor the changed conditions. For
this Purpose the relief valve may be set to operate in response to a limited pressure rise above the normal operatinghpressure. If the pressure should then rise, due, for example, to cutting out an atomizer, to the point at which the relief valve 20 is set to operate, the valve would serve to maintain this constant pressure across the pump and the system would operate as a constant differential system as represented by the curve 40 of Fig. 4 until the pressure again falls below the above mentioned point.
The above described method of operation in which the operating capacity of the atomizer is varied by regulating the oil return Q2 through control valve I5 may be termed wide range operation in contrast to a method of operation termed straight mechanical, in which there is no return and the supply pressure only is varied. In certain instances, however, it may be desired to operate this system over a part of the range as a. straight mechanical system in which no oil is returned through return line I 8. This may be accomplished by setting the relief valve 20 to produce a pressure dierential across the pump (Po-Pa) equal to that obtained with a given supply pressure Po when there is no iiow through return line I8. If the oil pressure P3 is then increased by actuation of the control valve I5, oil would tend to ilow to the atomizer through the return line Il. This, however, is prevented by check valve I9. Hence, there will b e no oil returned through the return line and the entire quantity of oil pumped by the hot oil pump will be discharged through the atomizer tip.
When thus operating in the straight mechanical' range, that is above point 28 in Fig. 3, the burner may have the characteristics represented by the curve 21 in Fig. 3. When the pressure on the Fig. 3.
The relief valve 20 may of course be connectedacross the lines I1 and I8 at or near the atomizers, if desired, so as to eliminate from consideration any variations in pressure in the lines themselves. In general, the connection of the relief valve between points near the atomizer will cause the curve 25 or 4U, representing the oil pumped to be more nearly horizontal, approaching curve 38 of Fig. 3. Connection of the valve at a point directly across the hot oil pump causes the operating curve 25 of Fig. 3 or 40 of Fig. 4 to be inclined due principally to the variation in pressure drop in the return line as the diierent quantities oi oil are withdrawn therethrough.
The system shown in Fig. 2 is similar to that described above and corresponding elements have been given corresponding reference numbers. In this embodiment, the hot oil pump 36 is of the type delivering a constant head regardless of the quantity. A valve 31 is shown as connected between the high Pressure Side 0f the hot oil pump 36 and the supply line I1. This valve constitutes, in effect, an adjustable xed orifice which reduces the 'pressure in the line I1. The purpose of the valve is to permit the system to be adjusted to maintain a given pressure differential between the supply and return lines without varying the hot oil pump itself should it not deliver the exact head required.
In operation, the hot oil pump 3B will be designed to maintain a pressure diierential greater than that desired between the supply and return lines. The pressure in the supply line is then reduced by means of the adjustable fixed oriice valve 31 so that the total pressure across the pump and the valve 31 becomes equal to that which it is desired to maintain between the supply and return lines. The system will then operate in accordance with the curves of Figs. 3 and 4 as above described.
It will be noted that the above described systems are simple to operate and require a minimum amount of equipment. They are adapted to the operation of single atomizers or'of a plurality of atomizers in parallel. Of course, if a source of high pressure oil supply is available, the pump II may be omitted. The preheater I2 may likewise be omitted, if desired, without changing the operation of the present system.
The pump II maintains a positive pressure on the low pressure side of the pump I6 and in the return line I8. Hence, the hot oil is maintained under'a head at all times and the tendency for a vapor lock to Iormband interfere with the operation of the system is avoided.
Although certain specic embodiments of the invention have been shown for purposes of illustration, it is to be understood that the invention is capable of various uses and that various changes and modifications may be made therein as will be readily apparent to a person skilled in the art. Certain specific terms have been used herein for convenience in referring to various details of the invention. These terms are, however, to be given as broad an interpretation as the state of the art will permit. 'I'he invention is only to be limited in accordance with the following claims.
What is claimed is:
1. A fluid atomizing system comprising an atomizer of the variable return type having a tip provided with a whirling chamber in which a rotary movement is imparted to the fluid and having an orice from which part of the rotating fluid is discharged for atomization, a supply conduit connected to suply fluid to said whirling chamber, a return conduit connected to withdraw a portion of the rotating fluid from said whirling chamber, constant pressure differential pump means connected to receive iiuid from said return conduit and to discharge said fluid to said supply conduit at a predetermined constant increase in pressure to thereby maintain a constant pressure differential between said supply and return conduits, a feed conduit connected to supply to said return conduit fluid to be atommized and to control the iluid pressure in said return conduit, and means to control the fiuid pressure in said feed conduit to thereby vary the capacity of said atomizer while maintaining by means of said pump means a. predetermined pressure differential between said supply'and return conduits.
2. In a iluid atomizing system as set forth in claim 1, a control valve connected between the high and low pressure sides olf said pump, said valve maintaining a. substantially constant pressure diierentialtherebetween.
3. A uid atomizing system as set forth in claim 1 in which said pump is of the positive displacement ty-pe. 1
4. A fluid atomizing system as set forth in claim 1, in which said pump is of the positive displacement type, and an adjustable lay-pass means isprovided between the high and low pressure sides of said pump suited to adjust the maximum capacity of said pump to the maximum 'capacity of the atomizer tip.
5. A fluid atomizing system as set forth in claim 1 in which a pump is included in said feed conduit to maintain a positive pressure on the low pressure side of said constant pressure differential pump suited to avoid vapor lock and a. valve is provided in said feed line to control the pressure of the fluid supplied to said return line.
6. In a fluid atomizing system as set forth in claim l, a check valve in said return conduit to prevent reverse flow of iluid therein to said atomlzer tip, whereby straight mechanical opera-- tion without uid return is obtained when the .pressure in said feed conduit is higher than the pressure in said tip.
7. The method of controlling the capacity of a variable return atomizer of the type having an atomizing tip provided with a whirling chamber in which a rotary movement is imparted to the iiuid and having an orifice from which part of the rotating fluid is discharged for atomization and having a fluid supply conduit to and a fluid return conduit Ifrom said whirling chamber and constant .pressure diierential pump means connected therebetween to recirculate the returned fluid, which method comprises supplying the fiuid from a source to the low pressure side of said pump and varying the atomizer capacity by controlling the pressure of said source while maintaining, by means of said pump means, a constant pressure differential between the su-pply and return conduits.
8. The method of controlling the capacity of a variable return atomizer of the type having an atomizing tip provided .with a whirling chamber in which a rotary movement is imparted to the uid and having an orifice from which all or a part of the rotating fluid is discharged for -atomization and having a fluid supply conduit to and a fluid return conduit from said whirling chamber and a pump connected therebetween to reclrculate the returned fluid, which` method comprises limiting the pressure differential across said pump to a predetermined amount,
vsupplying the fluid from a source to said pump and varying-the pressure of said source to thereby obtain straight mechanical operation without return from said whirling chamber when the pressure drop across said atomizing tip is greater than the pressure differential access said pump and to obtain wide range operation with fluid returned from said whirling chamber when the pressure drop across saidatomizing tip is equal to the pressure differential across said pump.
9. The method of controlling the burner output of a mechanically atomizing oil burner forming .part od a closed oil circulating system including the said burner, a pump for pumping oil to said burner, an oil supply line from said pump to saidl burner and an oil return line from said burner to said pump, comprising, utilizing a constant volume pump having a capacity greater than that required, by-passing around said pump a predetermined portion of the oil pumped, supplying to the said burners the constant volume of oil not lay-passed, returning excess oil not burned through an unrestricted return line, supplying oil to said system to make u-p the quantity of oil burned, and controlling the quantity of oil burned by regulating the quantity of make-.up oil supplied.
1o. Method of contrening the liquid sprayed .by a mechanical atomizer of the type wherein liquid is supplied to the atomizer tip at a ilow in excess of that at which said liquid is atomized, which comprises. establishing a constant volume flow from a pump to said atomizer at a value in excess of that at which liquid is atomized by said atomizer, recirculating excess ilow backl to said pump in a closed circulating system, supplying make-up liquid from a source of liquid to said circulating system, and controlling the quantity of liquid atomized by regulating the flow of make-up liquid to said circulating system at a point intermediate said source and said circulating system.'
ALBERT-P. OLCHZES.
y clazR'lIFIcmE'v oF coRREcT1oN.'. Patent m. 2,290,550. July 21, 19u2.
ALBERT -P. oLcHEs.
It is hereby -oertified that error-appears in the printed specification of the above numbered petentreciuiring correction as -fllowsg Page 5, avec-- one. c'olumn, line 50, Vfor suply readH--supply--I'g page I4, :second column, line 10, c1aix'n'8,`for access'f read a.cross' and that the said Letters Patent should beraad with this correotion 'therein that the same may con-- form to the record of the case i-n the Patent,.0fi`ice.`
Signed and sealedthis 1st day of September, A. D. 1911.2.'-
. l A Henry Van Arsdale, (Saai) Ating Commissioner of Patents.
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Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2436815A (en) * 1944-03-15 1948-03-02 Gen Electric Pressure operated valve
US2484580A (en) * 1944-12-11 1949-10-11 Overton Glen Feed distributor
US2566734A (en) * 1946-10-25 1951-09-04 Lucas Ltd Joseph Liquid fuel combustion system
US2592132A (en) * 1944-06-08 1952-04-08 Power Jets Res & Dev Ltd Liquid fuel supply and control system for atomizing nozzles
US2594992A (en) * 1950-01-10 1952-04-29 John P Quarles Pressure spray apparatus
US2702590A (en) * 1949-09-08 1955-02-22 Eloise B Stillman Liquid fuel circulating system for mechanically atomizing liquid fuel burner and method of controlling the output of said burner
US2702591A (en) * 1955-02-22 dickey
US2720256A (en) * 1950-05-12 1955-10-11 Rolls Royce Fuel systems for internal combustion engines and fuel pressurizing pumps therefor
US2730167A (en) * 1950-03-08 1956-01-10 Chrysler Corp Control apparatus
US2874766A (en) * 1954-07-07 1959-02-24 Dowty Fuel Syst Ltd Liquid fuel supply systems for gas turbine engines
US2990117A (en) * 1959-10-30 1961-06-27 American Air Filter Co Air heater fuel control system
US3037707A (en) * 1959-09-22 1962-06-05 Charles B Ligon Car washing apparatus
US3163360A (en) * 1962-12-26 1964-12-29 Vilbiss Co Airless spray gun utilizing low pressure coating material source
US3177919A (en) * 1960-09-30 1965-04-13 Clayton Manufacturing Co Method of and apparatus for removing nonliquid constituents from fuel oil
US3327760A (en) * 1965-09-01 1967-06-27 Orday Tool & Engineering Co In Fuel bypass control for automotive vehicle
US3348774A (en) * 1965-03-18 1967-10-24 Gyromat Corp Semi-automatic color change system for paint spray installation
US3458133A (en) * 1965-03-18 1969-07-29 Gyromat Corp Purging system for a spray painting installation
US4653532A (en) * 1985-11-18 1987-03-31 Graco Inc. Loop injection circulation system
US4771945A (en) * 1987-04-03 1988-09-20 Engineered Air Systems, Inc. Decontamination apparatus and method

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2702591A (en) * 1955-02-22 dickey
US2436815A (en) * 1944-03-15 1948-03-02 Gen Electric Pressure operated valve
US2592132A (en) * 1944-06-08 1952-04-08 Power Jets Res & Dev Ltd Liquid fuel supply and control system for atomizing nozzles
US2484580A (en) * 1944-12-11 1949-10-11 Overton Glen Feed distributor
US2566734A (en) * 1946-10-25 1951-09-04 Lucas Ltd Joseph Liquid fuel combustion system
US2702590A (en) * 1949-09-08 1955-02-22 Eloise B Stillman Liquid fuel circulating system for mechanically atomizing liquid fuel burner and method of controlling the output of said burner
US2594992A (en) * 1950-01-10 1952-04-29 John P Quarles Pressure spray apparatus
US2730167A (en) * 1950-03-08 1956-01-10 Chrysler Corp Control apparatus
US2720256A (en) * 1950-05-12 1955-10-11 Rolls Royce Fuel systems for internal combustion engines and fuel pressurizing pumps therefor
US2874766A (en) * 1954-07-07 1959-02-24 Dowty Fuel Syst Ltd Liquid fuel supply systems for gas turbine engines
US3037707A (en) * 1959-09-22 1962-06-05 Charles B Ligon Car washing apparatus
US2990117A (en) * 1959-10-30 1961-06-27 American Air Filter Co Air heater fuel control system
US3177919A (en) * 1960-09-30 1965-04-13 Clayton Manufacturing Co Method of and apparatus for removing nonliquid constituents from fuel oil
US3163360A (en) * 1962-12-26 1964-12-29 Vilbiss Co Airless spray gun utilizing low pressure coating material source
US3348774A (en) * 1965-03-18 1967-10-24 Gyromat Corp Semi-automatic color change system for paint spray installation
US3458133A (en) * 1965-03-18 1969-07-29 Gyromat Corp Purging system for a spray painting installation
US3327760A (en) * 1965-09-01 1967-06-27 Orday Tool & Engineering Co In Fuel bypass control for automotive vehicle
US4653532A (en) * 1985-11-18 1987-03-31 Graco Inc. Loop injection circulation system
US4771945A (en) * 1987-04-03 1988-09-20 Engineered Air Systems, Inc. Decontamination apparatus and method

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