US2319591A - Method of treating imperfectly combustible liquids or semiliquids - Google Patents
Method of treating imperfectly combustible liquids or semiliquids Download PDFInfo
- Publication number
- US2319591A US2319591A US392631A US39263141A US2319591A US 2319591 A US2319591 A US 2319591A US 392631 A US392631 A US 392631A US 39263141 A US39263141 A US 39263141A US 2319591 A US2319591 A US 2319591A
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- United States
- Prior art keywords
- fuel
- imperfectly
- treating
- liquid
- combustible
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000007788 liquid Substances 0.000 title description 26
- 238000000034 method Methods 0.000 title description 11
- 239000000446 fuel Substances 0.000 description 28
- 238000002485 combustion reaction Methods 0.000 description 10
- 239000000295 fuel oil Substances 0.000 description 9
- 239000003921 oil Substances 0.000 description 8
- 239000000203 mixture Substances 0.000 description 7
- 239000000126 substance Substances 0.000 description 5
- 230000001276 controlling effect Effects 0.000 description 4
- 230000001105 regulatory effect Effects 0.000 description 4
- 239000002131 composite material Substances 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 239000002253 acid Substances 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- AYFVYJQAPQTCCC-GBXIJSLDSA-N L-threonine Chemical compound C[C@@H](O)[C@H](N)C(O)=O AYFVYJQAPQTCCC-GBXIJSLDSA-N 0.000 description 1
- 239000004264 Petrolatum Substances 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 238000000889 atomisation Methods 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 239000002817 coal dust Substances 0.000 description 1
- 230000002939 deleterious effect Effects 0.000 description 1
- 239000003925 fat Substances 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000010742 number 1 fuel oil Substances 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 229940066842 petrolatum Drugs 0.000 description 1
- 235000019271 petrolatum Nutrition 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000012169 petroleum derived wax Substances 0.000 description 1
- 238000005504 petroleum refining Methods 0.000 description 1
- 235000019381 petroleum wax Nutrition 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 239000011299 tars and pitches Substances 0.000 description 1
- 239000000341 volatile oil Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D11/00—Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space
- F23D11/10—Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space the spraying being induced by a gaseous medium, e.g. water vapour
- F23D11/101—Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space the spraying being induced by a gaseous medium, e.g. water vapour medium and fuel meeting before the burner outlet
- F23D11/102—Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space the spraying being induced by a gaseous medium, e.g. water vapour medium and fuel meeting before the burner outlet in an internal mixing chamber
Definitions
- the invention relates to an improved method of treating imperfectly combustible liquids.
- the object is to deliver simultaneously two or more liquids in such manner that the more perfectly combustible liquid will facilitate the complete combustion or consumption of liquid or semi-liquid which is less perfectly or lesscompletely combustible, and thus prevent the clogging of the burner, or passages leading thereto, by substances which are normally non-combustible.
- the invention also comprises a method whereby undesirable constituents of the liquid are consumed, and thus prevented from contaminating the surrounding atmosphere.
- the invention also comprises the method whereby fuel oil is delivered into a substantially closed chamber, and an adjusted counterbalancing pressure is created in the chamber to modify the delivering of said oil to a combustion zone.
- the invention also comprises the method of treating an imperfectly combustible liquid or semi-liquid by introducing said liquid into a substantially closed chamber, simultaneously introducing into said chamber a fuel oil, and regulating or controlling the flow of the fuel oil by creating and maintaining an adjustable counterbalancing pressure in said chamber by the introduction thereto of compressed air or steam.
- colloidal fuels comprising a mixture of coal dust and oil.
- Fig. 1 is a longitudinal section of a well-known type of oil burner, which, with slight modifications, has been found suitable for realizing my object.
- Fig. 2 is a cross-section on line 2-2 of Fig. 1,
- Fig. 3 is a detail of a valve provided with an indicator scale.
- Fig. 1 the burner tip 5 is shown projecting into the combustion space i through a wall 'i of a furnace or the like.
- Fig. 2 shows three inlets ll, 58 and i9 associated with the burner body i2, for the purpose herein described.
- An inlet 20 is also provided for the atomizing medium, such as steam.
- the burner tip 5 is provided with the slot or opening 8, through which the atomized fuel is projected into the combustion space 0:.” zone.
- This opening or vent 8 is shaped suitably for the shape of the flame desiredflat, round or coneshaped.
- the flat flame tip has given the best results with the greatest variety of fuels.
- the thre inlets delivering to chamber 16 are as follows; the inlet I! for liquid fuel, the inlet I8 for more readily combustible fluid, and the inlet I9 for compressed air or gas.
- the atomizing medium such as steam
- nozzle i l which projects into the annular flange I0, is spaced from the flange so as to provide an annular channel between chamber 16 and passage 9.
- valves similar to that shown in Fig. 3, are provided for each of the respective inlets, for controlling the flows therethrough. These valves are preferably provided with indicator scales as shown in said Fig. 3, whereby said valves may be adjusted to secure the relative flows to suit the respective combustion characteristics of the sev-- eral mediums.
- the important features of the method are the simultaneous introduction of the different mediums in proper relative volumes, into a space such as chamber is for thorough mixing therein.
- the composite mixture then delivers to passage 9 for atomization and prompt delivery to the burner tip, before any accumulation of deleterious substances can take place.
- the two liquid fuels may be introduced into :1
- chamber I 6 under relatively low pressure or they may be under vacuum pressure due to the syphonin'g or induction action of the atcinizing jet through nozzle I l
- difficulty is frequently experienced in maintaining a constant rate of fuel flow to the combustion zone because of the presence of larger particles of coke or other solid matter in the fuel causing a clogging of the port opening in the valve controlling inlet l'l, especially at the lower ratings.
- valve controlled inlet as at I9, in a volume substantially equal to the amount of reduction in capacity required; that is, by admitting air to reduce the percentage of the maximum burning rate that is not needed.
- the burner is of such size as to have a maximum capacity of '75 U. S. gallons, or equal to ten cubic feet of oil per hour at pounds pressure, and it is desired to reduce the burning rate by one-half or to 37 gallons per hour, it is only necessary to admit compressed air at a rate of approximately five cubic feet per hour through port Hi.
- This air would usually be supplied at a slightly higher pressure than that of the oil, perhaps two pounds higher. Since air can be supplied physically clean, it can be accurately regulated in either larger or smaller volumes manually, or by some system of automatic control actuated by pressure or temperature variation of the heat absorbing vessel.
- the volume of air required fluctuated from to of the reduction in the volume of the fuel, depending on such factors as the relative temperature and pressures of the air and fuel.
- the supply of low volatile fuel may suddenly cease, which is often the case, the operator may then Wish to substitute a dirty, cokey fuel which has a high heat, high volatile value. Therefore, he does not need any of the supplementary fuel oil, but he does, because of the coke, need some means of control other than a fuel valve. In this case, the compressed air admitted through port l9 would be used to retard or control the flow of the cokey fuel to the burner, as above indicated.
Description
y 1943 w. FERGUSON 2,319,591
METHOD OF TREATING IMPEBFECTLY- QOMBUSTIBLE mourns on SEMI-LIQUIDS Filed May 9, 1941 Inderdon.
no net heating value.
Patented May 18, 1943 f METHOD OF TREATING IMPERFECTLY COMIBUSTIBLE LIQUIDS OR SEMILIQUIDS William Ferguson, Philadelphia, Pa., assignor to National Airoil Burner Company, Incorporated, a corporation of Delaware ApplicationMay 9, 1941, Serial No. 392,631
2 Claims.
The invention relates to an improved method of treating imperfectly combustible liquids.
The object is to deliver simultaneously two or more liquids in such manner that the more perfectly combustible liquid will facilitate the complete combustion or consumption of liquid or semi-liquid which is less perfectly or lesscompletely combustible, and thus prevent the clogging of the burner, or passages leading thereto, by substances which are normally non-combustible.
The invention also comprises a method whereby undesirable constituents of the liquid are consumed, and thus prevented from contaminating the surrounding atmosphere.
The invention also comprises the method whereby fuel oil is delivered into a substantially closed chamber, and an adjusted counterbalancing pressure is created in the chamber to modify the delivering of said oil to a combustion zone.
The invention also comprises the method of treating an imperfectly combustible liquid or semi-liquid by introducing said liquid into a substantially closed chamber, simultaneously introducing into said chamber a fuel oil, and regulating or controlling the flow of the fuel oil by creating and maintaining an adjustable counterbalancing pressure in said chamber by the introduction thereto of compressed air or steam.
In numerous and varied industries, certain. by- 1 product or waste liquors are available, some as semi-liquids, which have in several cases little or In some the flash point or ignition temperature is so high as to require the use of a supplementary fuel of. a more volatile character to sustain combustion. In others the primary object is one of disposing by heat of such undesirable constituents as acid and alkali residuums obtained from petroleum refining processes, also refuse products from chemical plants which, if not properly consumed in a furnace, will contaminate the surrounding atmosphere with obnoxious fumes.
Among the by-products fuels, semi-fuels, and refuses are (most of which are liquids or semi liquids):
Sludges from the bottoms of oil storage tanks.
Some sludges from sewerage plants.
Paper mill liquors.
So-called colloidal fuels comprising a mixture of coal dust and oil.
Petrolatum or petroleum wax.
Spent cutting and 1ubricating oils.
Tars and pitches from petroleum refineries, gas works, and wood chemical plants.
Waste liquid greases, fats, and oils from. paint works, chemical plants, soap factories and abattoirs.
Although some of these by-products can be burned satisfactorily by first mixing them in the storage tank with a more volatile oil such as the commercial grades of fuel oil either hot or cold, this introduces certain disadvantages such as the necessity of continuous agitation to keep the fuels well mixed to avoid sedimentation, precipitation, and coagulation. Another objection is the cost of the relatively expensive commercial fuel oil for blending. A few of the refuse fuels are not soluble in the commercial oil.
In the drawing, which shows by way of example, a suitable device for utilizing the invention;
Fig. 1 is a longitudinal section of a well-known type of oil burner, which, with slight modifications, has been found suitable for realizing my object.
Fig. 2 is a cross-section on line 2-2 of Fig. 1,
Fig. 3 is a detail of a valve provided with an indicator scale.
Similar numerals refer throughout the several views.
In Fig. 1, the burner tip 5 is shown projecting into the combustion space i through a wall 'i of a furnace or the like.
Fig. 2 shows three inlets ll, 58 and i9 associated with the burner body i2, for the purpose herein described.
An inlet 20 is also provided for the atomizing medium, such as steam.
The burner tip 5 is provided with the slot or opening 8, through which the atomized fuel is projected into the combustion space 0:." zone. This opening or vent 8 is shaped suitably for the shape of the flame desiredflat, round or coneshaped. The flat flame tip has given the best results with the greatest variety of fuels.
The thre inlets delivering to chamber 16, are as follows; the inlet I! for liquid fuel, the inlet I8 for more readily combustible fluid, and the inlet I9 for compressed air or gas.
At the rear of the burner body I2, is also provided the inlet 29 for the atomizing medium, such as steam, which is projected through nozzle H into passage 9 where the mediums become atomized to issue through opening 8 into the combustion zone.
It will be noted that nozzle i l, which projects into the annular flange I0, is spaced from the flange so as to provide an annular channel between chamber 16 and passage 9.
to similar parts Suitable valves similar to that shown in Fig. 3, are provided for each of the respective inlets, for controlling the flows therethrough. These valves are preferably provided with indicator scales as shown in said Fig. 3, whereby said valves may be adjusted to secure the relative flows to suit the respective combustion characteristics of the sev-- eral mediums.
The important features of the method are the simultaneous introduction of the different mediums in proper relative volumes, into a space such as chamber is for thorough mixing therein. The composite mixture then delivers to passage 9 for atomization and prompt delivery to the burner tip, before any accumulation of deleterious substances can take place.
The adjustment of the flows through ports [1, l8 and i9 will depend upon the specific characteristics of the refuse and of the fuel oil.
The two liquid fuels may be introduced into :1
chamber I 6 under relatively low pressure or they may be under vacuum pressure due to the syphonin'g or induction action of the atcinizing jet through nozzle I l In the burning of some residuum, refuse and composite fuels of liquid or semi-liquid characteristics, difficulty is frequently experienced in maintaining a constant rate of fuel flow to the combustion zone because of the presence of larger particles of coke or other solid matter in the fuel causing a clogging of the port opening in the valve controlling inlet l'l, especially at the lower ratings. I have found that satisfactory results may be achieved by having this valve opened wide for the maximum desired burning rate with a commensurate fuel pressure that may be as high as two hundred pounds or as low as two pounds per square inch, although twenty-five pounds would seem to be the most satisfactory for a commercial installation of a normal type.
Since a burner, in practice, necessarily must work through a wide range of capacity, say from a maximum rate down to 10% of this maximum, it becomes necessary to adjust the flow of fuel Without incurring the trouble caused by the solid particles clogging the opening of the valve at the lower rate.
For this purpose I reduce said maximum flow of fuel by admitting a fluid, such as compressed air, from any convenient source of supply, not
shown, through a valve controlled inlet, as at I9, in a volume substantially equal to the amount of reduction in capacity required; that is, by admitting air to reduce the percentage of the maximum burning rate that is not needed.
In other words, assuming that the burner is of such size as to have a maximum capacity of '75 U. S. gallons, or equal to ten cubic feet of oil per hour at pounds pressure, and it is desired to reduce the burning rate by one-half or to 37 gallons per hour, it is only necessary to admit compressed air at a rate of approximately five cubic feet per hour through port Hi. This air would usually be supplied at a slightly higher pressure than that of the oil, perhaps two pounds higher. Since air can be supplied physically clean, it can be accurately regulated in either larger or smaller volumes manually, or by some system of automatic control actuated by pressure or temperature variation of the heat absorbing vessel.
In my practice of the invention, the volume of air required fluctuated from to of the reduction in the volume of the fuel, depending on such factors as the relative temperature and pressures of the air and fuel. I have also had encouraging results when using a combustible gas in place of air as the regulating medium through port I 9.
Taking for example, the case where a nonvolatile acid fuel refuse is being admitted to the burner at the same time that good fuel is being admitted in the same proportion: when it is necessary to reduce the total amount of the composite fuels to the burner, some compressed air may be admitted through port Hi to reduce the flow of fuels simultaneously without necessitating individual readjustment of each of the two fuel valves.
On the same installation, the supply of low volatile fuel may suddenly cease, which is often the case, the operator may then Wish to substitute a dirty, cokey fuel which has a high heat, high volatile value. Therefore, he does not need any of the supplementary fuel oil, but he does, because of the coke, need some means of control other than a fuel valve. In this case, the compressed air admitted through port l9 would be used to retard or control the flow of the cokey fuel to the burner, as above indicated.
What I claim is:
1. The method of treating imperfectly combustible liquid, which consists in the simultaneous introduction, into a substantially closed chamber, of the imperfectly combustible liquid, a fuel oil, and a gaseous medium, to form a mixture in said chamber, and projecting a stream of atomizing medium to act inductively upon the mixture in the chamber in causing the projection of the mixture to a place of combustion.
2. The method of treating imperfectly combustible liquid or semi-liquid, which consists in the simultaneous introduction, into a substantially closed chamber, of the imperfectly combustible liquid, a fuel oil, and a gaseous medium to form a mixture in said chamber, controlling the flow of the liquid fuel by regulating the fiow of said gaseous medium, and projecting a stream of atomizing medium under pressure to act inductively in causing the projection of the mixture to a place of combustion.
WILLIAM FERGUSON.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US392631A US2319591A (en) | 1941-05-09 | 1941-05-09 | Method of treating imperfectly combustible liquids or semiliquids |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US392631A US2319591A (en) | 1941-05-09 | 1941-05-09 | Method of treating imperfectly combustible liquids or semiliquids |
Publications (1)
Publication Number | Publication Date |
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US2319591A true US2319591A (en) | 1943-05-18 |
Family
ID=23551382
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Application Number | Title | Priority Date | Filing Date |
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US392631A Expired - Lifetime US2319591A (en) | 1941-05-09 | 1941-05-09 | Method of treating imperfectly combustible liquids or semiliquids |
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Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2625141A (en) * | 1948-08-07 | 1953-01-13 | Martin J Berlyn | Fuel injection method |
US2625436A (en) * | 1948-08-07 | 1953-01-13 | Martin J Berlyn | Fuel injection apparatus |
US2760821A (en) * | 1954-04-05 | 1956-08-28 | Alfred L Kenworthy | Compound spray nozzles |
US2822038A (en) * | 1952-01-30 | 1958-02-04 | Nekoosa Edwards Paper Co | Treatment of residual waste liquor from sulphite process of making pulp |
US3903813A (en) * | 1974-05-28 | 1975-09-09 | Colt Ind Operating Corp | Method and apparatus for incinerating sludge |
WO1984001421A1 (en) * | 1982-09-27 | 1984-04-12 | Otis Eng Co | Burner |
US4655706A (en) * | 1982-09-27 | 1987-04-07 | Otis Engineering Corporation | Burner |
WO1995012091A1 (en) * | 1993-10-25 | 1995-05-04 | Liu, Wenwu | Pre-mixing combustion method and burner |
EP0698418A3 (en) * | 1994-08-26 | 1996-11-20 | Bayer Ag | Method and apparatus for simultaneously dispersing and spraying of at least two fluids |
US6128894A (en) * | 1996-12-19 | 2000-10-10 | Asea Brown Boveri Ag | Method of operating a burner |
-
1941
- 1941-05-09 US US392631A patent/US2319591A/en not_active Expired - Lifetime
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2625141A (en) * | 1948-08-07 | 1953-01-13 | Martin J Berlyn | Fuel injection method |
US2625436A (en) * | 1948-08-07 | 1953-01-13 | Martin J Berlyn | Fuel injection apparatus |
US2822038A (en) * | 1952-01-30 | 1958-02-04 | Nekoosa Edwards Paper Co | Treatment of residual waste liquor from sulphite process of making pulp |
US2760821A (en) * | 1954-04-05 | 1956-08-28 | Alfred L Kenworthy | Compound spray nozzles |
US3903813A (en) * | 1974-05-28 | 1975-09-09 | Colt Ind Operating Corp | Method and apparatus for incinerating sludge |
WO1984001421A1 (en) * | 1982-09-27 | 1984-04-12 | Otis Eng Co | Burner |
US4655706A (en) * | 1982-09-27 | 1987-04-07 | Otis Engineering Corporation | Burner |
WO1995012091A1 (en) * | 1993-10-25 | 1995-05-04 | Liu, Wenwu | Pre-mixing combustion method and burner |
EP0698418A3 (en) * | 1994-08-26 | 1996-11-20 | Bayer Ag | Method and apparatus for simultaneously dispersing and spraying of at least two fluids |
US5639024A (en) * | 1994-08-26 | 1997-06-17 | Bayer Aktiengesellschaft | Method and device for the simultaneous dispersion and atomisation of at least two liquids |
US6128894A (en) * | 1996-12-19 | 2000-10-10 | Asea Brown Boveri Ag | Method of operating a burner |
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