US3662717A - Waste-heat boiler - Google Patents
Waste-heat boiler Download PDFInfo
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- US3662717A US3662717A US102588A US10258870A US3662717A US 3662717 A US3662717 A US 3662717A US 102588 A US102588 A US 102588A US 10258870 A US10258870 A US 10258870A US 3662717 A US3662717 A US 3662717A
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- coolant
- tubes
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- heat boiler
- ejectors
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- 239000002918 waste heat Substances 0.000 title claims abstract description 40
- 239000002826 coolant Substances 0.000 claims abstract description 52
- 239000007789 gas Substances 0.000 claims abstract description 25
- 239000007921 spray Substances 0.000 claims abstract description 21
- 239000007788 liquid Substances 0.000 claims abstract description 11
- 238000007599 discharging Methods 0.000 claims description 2
- 238000001816 cooling Methods 0.000 abstract description 11
- 229930195733 hydrocarbon Natural products 0.000 description 5
- 150000002430 hydrocarbons Chemical class 0.000 description 5
- 238000002485 combustion reaction Methods 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 239000004071 soot Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- -1 for example Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 231100001261 hazardous Toxicity 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
Images
Classifications
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/04—Purifying combustible gases containing carbon monoxide by cooling to condense non-gaseous materials
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
- C01B3/36—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using oxygen or mixtures containing oxygen as gasifying agents
- C01B3/363—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using oxygen or mixtures containing oxygen as gasifying agents characterised by the burner used
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/02—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled
- F28D7/024—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled the conduits of only one medium being helically coiled tubes, the coils having a cylindrical configuration
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
Definitions
- ABSTRACT An improved waste-heat boiler for cooling and recovering heat from hot gases.
- the improvement comprises employing two concentric tubes for delivering coolant liquid, the coolant liquid from the innerconcentric tube under pressure serving as feed to a plurality of ejectors which draw coolant liquid from the outer concentric tube and by means of an arrangement of spray nozzle arms, direct the coolant against the bottom plate of the boiler and the inlet ends of the heat exchange tubes connected thereto.
- This invention relates to an improved apparatus for cooling and abstracting heat from high temperature gases with the generation of steam at superatmospheric pressures, e.g., pressures of from 5-l50 atmospheres.
- the waste-heat boiler herein provided is particularly suitable for the recovery of sen sible heat from hot, soot-containing gases obtained by partial combustion of hydrocarbons with oxygen or oxygen-enriched air, e.g., hydrogen and carbon monoxide-containing synthesis gas obtained from an oil gasification process.
- Crude synthesis gas produced by the partial combustion of hydrocarbons generally is discharged from the reactor at a temperature of from l,300 to 1,400 C. or higher, thus making it an obvious source of potential'energy.
- the thermal energy in synthesis gas can be recovered only with great difficulty utilizing conventional heat exchangers, because of the presence in such gas of large amounts of soot (i.e., free carbon), often up to 5 percent or more, which tends to deposit on the inside of the exchange tubes.
- soot i.e., free carbon
- Coolant liquid is normally admitted into the waste-heat boiler through a vertical, radially spaced tube which can be provided with a nozzle so that the coolant is discharged against the hot bottom plate, after which it ascends upward into the space formed between the coolant tube and the shell of the waste-heat boiler, thereby cooling the straight and/or helically coiled tube or tubes accommodated therein.
- the heat exchange tubes comprise two or more helically coiled tubes each connected to a straight tube through which the hot gas is initially flowed.
- the straight tubes may be of relatively short length and thus serve merely as connecting pieces, or may be selected longer, if desired, for constructional reasons or to reduce the temperature of the gases before they enter the first coil of the helically coiled tubes.
- a central ejector issuing vertically from the lower end of the inner concentric tube, together with at least one ancillary ejector issuing laterally from the lower end of said tube.
- the spray nozzle anns extending from the outer concentric tube will be positioned so as to cooperate with and receive coolant from the ejectors, and to direct coolant streams against the bottom plate and the inlet ends of the exchange tubes.
- the use of a central and plurality of ancillary ejectors and corresponding central and ancillary spray nozzle arms ensures even cooling of the bottom plate and inlet ends of the exchange tubes.
- the coolant in the outer concentric tube can be used to provide a measure of cooling even if the flow of coolant in the inner tube is interrupted. This can be conveniently accomplished, for example, by connecting the outer tube to a storage vessel containing coolant located above the waste-heat boiler, so that a continued supply of coolant is ensured even if coolant pressure in the inner tube should fail.
- the space of the waste-heat boiler in which the'ejector nozzle arrangement is accommodated has, at the point of connection of the ejectors and nozzles to the concentric tubes, a free cross-sectional area which does not exceed 30 percent of the space accommodating the helical coils. This results in an improved flow of the coolant through the waste-heat boiler.
- baffle plates which, for example, with'a waste-heat boiler having four straight tubes, may have the shape of a curved shield and bedisposed symmetrically along the wall of the space, the concave side facing the wall.
- the temperature of the gases to be cooled may be lowered by injecting a coolant, for example, water, into the gases after they have left the reaction chamber.
- a coolant for example, water
- This precooling of the gases may be carried out continuously or temporarily, for example, if difficulties should be encountered in supplying coolant to the waste-heat boiler.
- FIG. 1 is a diagrammatic representation of an apparatus for the partial combustion of hydrocarbons and the cooling thereof.
- FIG. 2 is a side view of an embodiment of the waste-heat boiler.
- FIG. 3 shows a cross section of an embodiment-of the wasteheat boiler through the space accommodating the straight tubes, i.e., immediately above the outflow point of the spray nozzle arms with which the ancillary ejectors cooperate.
- the waste-heat boiler depicted has four helical coils each connected to a straight tube.
- FIG. 4 shows a cross section of an embodiment of the wasteheat boiler through the space accommodating the straight tubes, i.e., at some distance above the level at which the ejector-nozzles are connected.
- the waste-heat boiler is provided with four helical coils each connected to a straight tube and with four baffle plates which are arranged in the space accommodating the straight tubes and which extend near to the bottom plate.
- part A represents a reactor for partially combusting hydrocarbons which is provided with fuel supply line q leading to burner part A of the reactor, and oxygen supply line b. Steam, if used, can be supplied through either q and/or b.
- Part B is a connection between the reactor and connecting piece C.
- the hot gases are passed through the connection B and the connecting piece to waste-heat boiler D which is provided with two straight tubes and two helical coils, discharges c and d for the cooled gases, inlets e and f for the coolant (e.g., water) and outlet k for the coolant.
- the straight tubes are designated by g and h, and the helical coils by i and j.
- FIG. 2 is a side view of a part of the embodiment of the waste-heat boiler.
- the waste-heat boiler comprises cylindrical vessel 1 having bottom plate 2, placed on connecting piece 3 which is provided with gas supply line 4.
- the waste-heat boiler further comprises concentric tubes 5 and 6 through which the coolant is supplied (under pressure in tube 6), the bottom ends of which are linked to a spray nozzle comprising central ejector 11 which cooperates with central arm 12 and two ancillary ejectors 7 and 8 which cooperate with arms 9 and 10, respectively.
- the coolant preferably water, is supplied through concentric tubes 5 and 6 and is sprayed against the bottom plate by the arms 9, l0 and 12, after which it flows upwards thereby cooling the straight tubes designated by 13 and 14.
- FIG. 3 is a cross section through the space accommodating the straight tubes, taken immediately above the discharge point of the spray nozzle arms of the embodiment shown in FIG. 2, but which has four helical coils, each connected to a straight tube.
- the cross section shows the four straight tubes, the central arm of the spray noule and the four arms with which the ancillary ejectors cooperate.
- reference numerals 21, 22, 23 and 24 designate the straight tubes
- 25 is the central arm of the spray nozzle
- 26, 27, 28 and 29 are the arms with which the ancillary ejectors cooperate.
- the outflowing coolant acquires a horizontal component of movement as a result of the lateral curvature of arms 26, 27, 28 and 29.
- FIG. 4 is a cross section through the space accommodating the straight tubes of an embodiment of the waste-heat boiler having the configuration shown in FIG. 3, but in which the cross section is taken at some distance above the point at which the ejector-nozzle arrangement is connected.
- the cross section shows the four straight tubes, the concentric tubes through which the coolant flows and the baffle plates for the coolant.
- the reference numerals 31, 32, 33 and 34 designate the straight tubes
- 35 is the inner tube through which the coolant flows under pressure
- 36 is the outer tube from which the coolant is drawn by the ejectors
- 37, 38, 39 and 40 are the baffle plates for the coolant.
- a waste-heat boiler for generating vapors from a coolant by heat transfer from a high temperature gas which comprises: (1) a closed vessel having a bottom plate and an outlet means for discharging vaporized and liquid coolant; (2) a plurality of straight tubes into which hot gas is introduced, each connected at its inlet end to the bottom plate and at its outlet end to a helically coiled tube through which the gas is flowed and discharged from an upper part of said vessel; (3) two vertical concentric tubes for supplying coolant liquid mounted within said vessel in a radially spaced relation thereto and defining with said vessel an elongated annular space in which said straight and helically coiled tubes are situated; (4) a central ejector and plurality of ancillary ejectors by means of which coolant is drawn from the outer of said concentric tubes, said ejectors issuing from the lower end of the inner of said concentric tubes and being fed by coolant supplied therefrom; (5) a central spray nozzle arm and plurality
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- Engineering & Computer Science (AREA)
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- Combustion & Propulsion (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- General Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- Inorganic Chemistry (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Industrial Gases (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
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Abstract
An improved waste-heat boiler for cooling and recovering heat from hot gases. The improvement comprises employing two concentric tubes for delivering coolant liquid, the coolant liquid from the inner concentric tube under pressure serving as feed to a plurality of ejectors which draw coolant liquid from the outer concentric tube and by means of an arrangement of spray nozzle arms, direct the coolant against the bottom plate of the boiler and the inlet ends of the heat exchange tubes connected thereto.
Description
United States Patent Ter Haar 51 May 16, 1972 [54] WASTE-HEAT BOILER Leonard W. Ter l-laar, Hague, Netherlands t [73] Assignee: Shell Oil Company, Houston, Tex.
[22] Filed: Dec. 30, 1970 [2]] App], No.: 102,588
[72] Inventor:
[30] Foreign Application Priority Data Jan. 21, 1970 Netherlands ..70008l2 [52] US. Cl. ..l22/7 R, 122/40 [51] Int. Cl ..F22b 1/18 [58] Field ofSearch ..l22/7 R, 40,4], 114
[56] References Cited UNITED STATES PATENTS 2,790,428 4/ 1957 Buttler 122/40 X 2,967,515 1/1961 Hofstede et al i 22/7 Primary Examiner-Kenneth W. Sprague AttorneyGlen R. Grunewald and John H. Colvin [57] ABSTRACT An improved waste-heat boiler for cooling and recovering heat from hot gases. The improvement comprises employing two concentric tubes for delivering coolant liquid, the coolant liquid from the innerconcentric tube under pressure serving as feed to a plurality of ejectors which draw coolant liquid from the outer concentric tube and by means of an arrangement of spray nozzle arms, direct the coolant against the bottom plate of the boiler and the inlet ends of the heat exchange tubes connected thereto.
5 Claims, 4 Drawing Figures PMENTEDmvsnsvz 3.662.717
SHEET 1 BF 2 B M J FIG. I
INVENTORI LEONARD w. TER VHAAR HIS ATTORNEY P'A'TENFEnm 16 m2 3.662.717
sum 2 BF 2 1 f /5 q 4 6 :I I3 4 IO N 2 9 FIG. 2
INVENTOR:
LEONARD W. TER HAAR FIG. 4 2;
, HIS ATTORNEY WASTE-HEAT BOILER BACKGROUND OF THE INVENTION 1 Field of the Invention This invention relates to an improved apparatus for cooling and abstracting heat from high temperature gases with the generation of steam at superatmospheric pressures, e.g., pressures of from 5-l50 atmospheres. The waste-heat boiler herein provided is particularly suitable for the recovery of sen sible heat from hot, soot-containing gases obtained by partial combustion of hydrocarbons with oxygen or oxygen-enriched air, e.g., hydrogen and carbon monoxide-containing synthesis gas obtained from an oil gasification process.
2. Description of the Prior Art Crude synthesis gas produced by the partial combustion of hydrocarbons generally is discharged from the reactor at a temperature of from l,300 to 1,400 C. or higher, thus making it an obvious source of potential'energy. The thermal energy in synthesis gas, however, can be recovered only with great difficulty utilizing conventional heat exchangers, because of the presence in such gas of large amounts of soot (i.e., free carbon), often up to 5 percent or more, which tends to deposit on the inside of the exchange tubes. A number of waste-heat boilers have been proposed forum in recovering heat from such gases, for example, the apparatus described in US. Pat. No. 2,967,515 to Hofstede et al. in which helically coiled tubes are employed, or that described in copending US. application Ser. No. 87,451, filed Nov. 6, 1970, in which a combination of straight and helically coiled heat exchange tubes are used. In boilers of this general design, hot gas obtained from the partial combustion of hydrocarbons is introduced into the waste-heat boiler and flowed through one or more straight and/or helically coiled tubes connected at their inlet ends to the bottom plate of the boiler. Coolant liquid is normally admitted into the waste-heat boiler through a vertical, radially spaced tube which can be provided with a nozzle so that the coolant is discharged against the hot bottom plate, after which it ascends upward into the space formed between the coolant tube and the shell of the waste-heat boiler, thereby cooling the straight and/or helically coiled tube or tubes accommodated therein. j
In view of the high temperatures to which the bottom plate and gas inlet ends of theheat exchange tubes are exposed, it is of obvious importance that these surfaces be adequately cooled. However, this has often proved to be difficult in prac tice, particularly in waste-heat boilers wherein a plurality of heat exchange tubes are connected to the bottom plate, because of the interference of the tubes with the coolant flow which results in uneven cooling. Conventional Waste-heat boilers equipped with a single coolant supply tube suffer from a further deficiency in that in the event of an interruption in the flow of coolant, e.g., because of an operational breakdown, high pressures and temperatures rapidly develop in the boiler creating a potentially hazardous situation. The present invention provides a means of overcoming these problems.
SUMMARY OF THE INVENTION It has now been found that the heat exchange tubes and bottom plate of a waste-heat boiler can be efficiently cooled by the use of two concentric cooling tubes connected to a novel ejector-nozzle arrangement as hereinafter described. A plurality of ejectors are employed in this arrangement, issuing from the inner of the above-mentioned concentric tubes. These ejectors are fed by coolant under pressure from the inner concentric tube and serve to draw coolant from the outer concentric tube. The coolant discharged from the ejectors and that drawn from the outer tube is directed by means of aplurality of spray nozzle arms against the bottom plate of the waste-heat boiler and the inlet ends of the heat exchange tubes, thereby cooling the same.
DESCRIPTION OF PREFERRED EMBODIMENTS In a preferred embodiment of the invention, the heat exchange tubes comprise two or more helically coiled tubes each connected to a straight tube through which the hot gas is initially flowed. The straight tubes may be of relatively short length and thus serve merely as connecting pieces, or may be selected longer, if desired, for constructional reasons or to reduce the temperature of the gases before they enter the first coil of the helically coiled tubes.
In one embodiment of the waste-heat boiler of the invention, a central ejector issuing vertically from the lower end of the inner concentric tube is employed, together with at least one ancillary ejector issuing laterally from the lower end of said tube. In this embodiment, the spray nozzle anns extending from the outer concentric tube will be positioned so as to cooperate with and receive coolant from the ejectors, and to direct coolant streams against the bottom plate and the inlet ends of the exchange tubes. The use of a central and plurality of ancillary ejectors and corresponding central and ancillary spray nozzle arms ensures even cooling of the bottom plate and inlet ends of the exchange tubes. This is particularly the case if the number of ancillary ejectors is equal to the number of straight tubes and these ejectors cooperate with the spray nozzle arms arranged symmetrically and issuing between the straight tubes. These arms are preferably curved in such a way that the outflowing coolant acquiresa direction of movement with a horizontal velocity component. I
In the aforedescribed embodiment, the coolant in the outer concentric tube can be used to provide a measure of cooling even if the flow of coolant in the inner tube is interrupted. This can be conveniently accomplished, for example, by connecting the outer tube to a storage vessel containing coolant located above the waste-heat boiler, so that a continued supply of coolant is ensured even if coolant pressure in the inner tube should fail.
In a specific embodiment of the apparatus, the space of the waste-heat boiler in which the'ejector nozzle arrangement is accommodated, has, at the point of connection of the ejectors and nozzles to the concentric tubes, a free cross-sectional area which does not exceed 30 percent of the space accommodating the helical coils. This results in an improved flow of the coolant through the waste-heat boiler. p
The above free cross-sectional area may be given the desired value by arranging baffle plates, which, for example, with'a waste-heat boiler having four straight tubes, may have the shape of a curved shield and bedisposed symmetrically along the wall of the space, the concave side facing the wall.
If desired, the temperature of the gases to be cooled may be lowered by injecting a coolant, for example, water, into the gases after they have left the reaction chamber. This precooling of the gases may be carried out continuously or temporarily, for example, if difficulties should be encountered in supplying coolant to the waste-heat boiler.
The invention will now be further explained with reference to the diagrammatic drawings, which illustrate different embodiments of the apparatus according to the invention.
FIG. 1 is a diagrammatic representation of an apparatus for the partial combustion of hydrocarbons and the cooling thereof.
FIG. 2 is a side view of an embodiment of the waste-heat boiler.
FIG. 3 shows a cross section of an embodiment-of the wasteheat boiler through the space accommodating the straight tubes, i.e., immediately above the outflow point of the spray nozzle arms with which the ancillary ejectors cooperate. The waste-heat boiler depicted has four helical coils each connected to a straight tube.
FIG. 4 shows a cross section of an embodiment of the wasteheat boiler through the space accommodating the straight tubes, i.e., at some distance above the level at which the ejector-nozzles are connected. The waste-heat boiler is provided with four helical coils each connected to a straight tube and with four baffle plates which are arranged in the space accommodating the straight tubes and which extend near to the bottom plate.
Referring now to FIG. 1, part A represents a reactor for partially combusting hydrocarbons which is provided with fuel supply line q leading to burner part A of the reactor, and oxygen supply line b. Steam, if used, can be supplied through either q and/or b. Part B is a connection between the reactor and connecting piece C. The hot gases are passed through the connection B and the connecting piece to waste-heat boiler D which is provided with two straight tubes and two helical coils, discharges c and d for the cooled gases, inlets e and f for the coolant (e.g., water) and outlet k for the coolant. The straight tubes are designated by g and h, and the helical coils by i and j.
FIG. 2 is a side view of a part of the embodiment of the waste-heat boiler. The waste-heat boiler comprises cylindrical vessel 1 having bottom plate 2, placed on connecting piece 3 which is provided with gas supply line 4. The waste-heat boiler further comprises concentric tubes 5 and 6 through which the coolant is supplied (under pressure in tube 6), the bottom ends of which are linked to a spray nozzle comprising central ejector 11 which cooperates with central arm 12 and two ancillary ejectors 7 and 8 which cooperate with arms 9 and 10, respectively. The coolant, preferably water, is supplied through concentric tubes 5 and 6 and is sprayed against the bottom plate by the arms 9, l0 and 12, after which it flows upwards thereby cooling the straight tubes designated by 13 and 14.
FIG. 3 is a cross section through the space accommodating the straight tubes, taken immediately above the discharge point of the spray nozzle arms of the embodiment shown in FIG. 2, but which has four helical coils, each connected to a straight tube. The cross section shows the four straight tubes, the central arm of the spray noule and the four arms with which the ancillary ejectors cooperate. In the drawing, reference numerals 21, 22, 23 and 24 designate the straight tubes, 25 is the central arm of the spray nozzle and 26, 27, 28 and 29 are the arms with which the ancillary ejectors cooperate. The outflowing coolant acquires a horizontal component of movement as a result of the lateral curvature of arms 26, 27, 28 and 29.
FIG. 4 is a cross section through the space accommodating the straight tubes of an embodiment of the waste-heat boiler having the configuration shown in FIG. 3, but in which the cross section is taken at some distance above the point at which the ejector-nozzle arrangement is connected. The cross section shows the four straight tubes, the concentric tubes through which the coolant flows and the baffle plates for the coolant. In the drawing the reference numerals 31, 32, 33 and 34 designate the straight tubes, 35 is the inner tube through which the coolant flows under pressure, 36 is the outer tube from which the coolant is drawn by the ejectors, and 37, 38, 39 and 40 are the baffle plates for the coolant.
I claim as my invention:
1. A waste-heat boiler for generating vapors from a coolant by heat transfer from a high temperature gas which comprises: (1) a closed vessel having a bottom plate and an outlet means for discharging vaporized and liquid coolant; (2) a plurality of straight tubes into which hot gas is introduced, each connected at its inlet end to the bottom plate and at its outlet end to a helically coiled tube through which the gas is flowed and discharged from an upper part of said vessel; (3) two vertical concentric tubes for supplying coolant liquid mounted within said vessel in a radially spaced relation thereto and defining with said vessel an elongated annular space in which said straight and helically coiled tubes are situated; (4) a central ejector and plurality of ancillary ejectors by means of which coolant is drawn from the outer of said concentric tubes, said ejectors issuing from the lower end of the inner of said concentric tubes and being fed by coolant supplied therefrom; (5) a central spray nozzle arm and plurality of ancillary spray nozzle arms extending from the lower end of the outer concentric tube, positioned so as to receive the coolant discharged from the e ector and drawn from the outer concentric tube, and
discharge the same against the bottom plate and the inlet ends of said straight tubes.
2. The waste-heat boiler of claim 1 wherein the number of ancillary ejectors is equal to the number of straight tubes and the ancillary spray nozzle arms are arranged symmetrically and issue between the straight tubes.
3. The waste-heat boiler of claim 2 wherein the spray nozzle arms are curved laterally so that the discharged coolant acquires a direction of movement with a horizontal velocity component.
4. The waste-heat boiler of claim 1 wherein the space at the point the ejectors and spray nozzle arms are connected to the concentric tubes has a free cross-sectional area of less than 30 percent of the space accommodating the helical coils.
5. The waste-heat boiler of claim 1 wherein baffle plates are present in the space accommodating the straight tubes.
Claims (5)
1. A waste-heat boiler for generating vapors from a coolant by heat transfer from a high temperature gas which comprises: (1) a closed vessel having a bottom plate and an outlet means for discharging vaporized and liquid coolant; (2) a plurality of straight tubes into which hot gas is introduced, each connected at its inlet end to the bottom plate and at its outlet end to a helically coiled tube through which the gas is flowed and discharged from an upper part of said vessel; (3) two vertical concentric tubes for supplying coolant liquid mounted within said vessel in a radially spaced relation thereto and defining with said vessel an elongated annular space in which said straight and helically coiled tubes are situated; (4) a central ejector and plurality of ancillary ejectors by means of which coolant is drawn from the outer of said concentric tubes, said ejectors issuing from the lower end of the inner of said concentric tubes and being fed by coolant supplied therefrom; (5) a central spray nozzle arm and plurality of ancillary spray nozzle arms extending from the lower end of the outer concentric tube, positioned so as to receive the coolant discharged from the ejector and drawn from the outer concentric tube, and discharge the same against the bottom plate and the inlet ends of said straight tubes.
2. The waste-heat boiler of claim 1 wherein the number of ancillary ejectors is equal to the number of straight tubes and the ancillary spray nozzle arms are arranged symmetrically and issue between the straight tubes.
3. The waste-heat boiler of claim 2 wherein the spray nozzle arms are curved laterally so that the discharged coolant acquires a direction of movement with a horizontal velocity component.
4. The waste-heat boiler of claim 1 wherein the space at the point the ejectors and spray nozzle arms are connected to the concentric tubes has a free cross-sectional area of less than 30 percent of the space accommodating the helical coils.
5. The waste-heat boiler of claim 1 wherein baffle plates are present in the space accommodating the straight tubes.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| NL7000812.A NL166905C (en) | 1970-01-21 | 1970-01-21 | APPARATUS FOR PREPARING AND COOLING A HYDROGEN AND CARBON MONOXIDE GAS MIX WITH A REACTION CHAMBER AND A HEAT EXCHANGER WITH AT LEAST PARTICULARLY INJURED PIPES. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3662717A true US3662717A (en) | 1972-05-16 |
Family
ID=19809144
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US102588A Expired - Lifetime US3662717A (en) | 1970-01-21 | 1970-12-30 | Waste-heat boiler |
Country Status (20)
| Country | Link |
|---|---|
| US (1) | US3662717A (en) |
| JP (1) | JPS5338274B1 (en) |
| AT (1) | AT319282B (en) |
| BE (1) | BE761460A (en) |
| CA (1) | CA938106A (en) |
| CH (1) | CH556797A (en) |
| CS (1) | CS171223B2 (en) |
| DE (1) | DE2102368C3 (en) |
| DK (1) | DK132615C (en) |
| ES (1) | ES387406A1 (en) |
| FI (1) | FI53829C (en) |
| FR (1) | FR2075714A5 (en) |
| GB (1) | GB1340254A (en) |
| IE (1) | IE34897B1 (en) |
| NL (1) | NL166905C (en) |
| NO (1) | NO132793C (en) |
| SE (1) | SE358618B (en) |
| SU (1) | SU473378A3 (en) |
| TR (1) | TR16781A (en) |
| ZA (1) | ZA71321B (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3788281A (en) * | 1972-03-27 | 1974-01-29 | Shell Oil Co | Process and waste-heat boiler for cooling soot-containing synthesis gas |
| US4029054A (en) * | 1975-01-17 | 1977-06-14 | Shell Oil Company | Waste heat boiler |
| US4243097A (en) * | 1975-08-27 | 1981-01-06 | Shell Oil Company | Waste heat boiler |
| US4270493A (en) * | 1979-01-08 | 1981-06-02 | Combustion Engineering, Inc. | Steam generating heat exchanger |
| US20090038155A1 (en) * | 2007-08-07 | 2009-02-12 | Judeth Helen Brannon Corry | Syngas coolers and methods for assembling same |
| US20090041642A1 (en) * | 2007-08-07 | 2009-02-12 | General Electric Company | Radiant coolers and methods for assembling same |
| US8269170B2 (en) | 2003-04-23 | 2012-09-18 | Battelle Memorial Institute | Methods and systems for remote detection of gases |
| US11807822B2 (en) * | 2019-02-05 | 2023-11-07 | Saudi Arabian Oil Company | Producing synthetic gas |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2790428A (en) * | 1952-12-23 | 1957-04-30 | Buttler John Allen | Instantaneous steam generators |
| US2967515A (en) * | 1956-12-21 | 1961-01-10 | Shell Oil Co | Waste-heat boiler |
-
1970
- 1970-01-21 NL NL7000812.A patent/NL166905C/en not_active IP Right Cessation
- 1970-12-30 US US102588A patent/US3662717A/en not_active Expired - Lifetime
-
1971
- 1971-01-12 BE BE761460A patent/BE761460A/en not_active IP Right Cessation
- 1971-01-19 CA CA103102A patent/CA938106A/en not_active Expired
- 1971-01-19 CS CS343A patent/CS171223B2/cs unknown
- 1971-01-19 ES ES387406A patent/ES387406A1/en not_active Expired
- 1971-01-19 TR TR16781A patent/TR16781A/en unknown
- 1971-01-19 GB GB255071A patent/GB1340254A/en not_active Expired
- 1971-01-19 CH CH74371A patent/CH556797A/en not_active IP Right Cessation
- 1971-01-19 IE IE58/71A patent/IE34897B1/en unknown
- 1971-01-19 FR FR7101671A patent/FR2075714A5/fr not_active Expired
- 1971-01-19 DE DE2102368A patent/DE2102368C3/en not_active Expired
- 1971-01-19 FI FI117/71A patent/FI53829C/en active
- 1971-01-19 ZA ZA710321A patent/ZA71321B/en unknown
- 1971-01-19 NO NO71184A patent/NO132793C/no unknown
- 1971-01-19 SU SU1611807A patent/SU473378A3/en active
- 1971-01-19 DK DK20071*#A patent/DK132615C/en not_active IP Right Cessation
- 1971-01-19 SE SE00591/71A patent/SE358618B/xx unknown
- 1971-01-19 JP JP118471A patent/JPS5338274B1/ja active Pending
- 1971-01-19 AT AT43071A patent/AT319282B/en active
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2790428A (en) * | 1952-12-23 | 1957-04-30 | Buttler John Allen | Instantaneous steam generators |
| US2967515A (en) * | 1956-12-21 | 1961-01-10 | Shell Oil Co | Waste-heat boiler |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3788281A (en) * | 1972-03-27 | 1974-01-29 | Shell Oil Co | Process and waste-heat boiler for cooling soot-containing synthesis gas |
| US4029054A (en) * | 1975-01-17 | 1977-06-14 | Shell Oil Company | Waste heat boiler |
| US4243097A (en) * | 1975-08-27 | 1981-01-06 | Shell Oil Company | Waste heat boiler |
| US4270493A (en) * | 1979-01-08 | 1981-06-02 | Combustion Engineering, Inc. | Steam generating heat exchanger |
| US8269170B2 (en) | 2003-04-23 | 2012-09-18 | Battelle Memorial Institute | Methods and systems for remote detection of gases |
| US20090038155A1 (en) * | 2007-08-07 | 2009-02-12 | Judeth Helen Brannon Corry | Syngas coolers and methods for assembling same |
| US20090041642A1 (en) * | 2007-08-07 | 2009-02-12 | General Electric Company | Radiant coolers and methods for assembling same |
| US8191617B2 (en) | 2007-08-07 | 2012-06-05 | General Electric Company | Syngas cooler and cooling tube for use in a syngas cooler |
| US8240366B2 (en) | 2007-08-07 | 2012-08-14 | General Electric Company | Radiant coolers and methods for assembling same |
| US11807822B2 (en) * | 2019-02-05 | 2023-11-07 | Saudi Arabian Oil Company | Producing synthetic gas |
Also Published As
| Publication number | Publication date |
|---|---|
| CS171223B2 (en) | 1976-10-29 |
| SU473378A3 (en) | 1975-06-05 |
| AT319282B (en) | 1974-12-10 |
| NL166905C (en) | 1981-10-15 |
| DE2102368A1 (en) | 1971-08-05 |
| NO132793B (en) | 1975-09-29 |
| DK132615C (en) | 1976-05-31 |
| ZA71321B (en) | 1971-10-27 |
| DK132615B (en) | 1976-01-12 |
| NL166905B (en) | 1981-05-15 |
| TR16781A (en) | 1973-05-01 |
| NO132793C (en) | 1976-01-07 |
| FI53829C (en) | 1978-08-10 |
| DE2102368C3 (en) | 1980-02-07 |
| FI53829B (en) | 1978-05-02 |
| GB1340254A (en) | 1973-12-12 |
| BE761460A (en) | 1971-07-12 |
| CH556797A (en) | 1974-12-13 |
| JPS5338274B1 (en) | 1978-10-14 |
| SE358618B (en) | 1973-08-06 |
| IE34897B1 (en) | 1975-09-17 |
| IE34897L (en) | 1971-07-21 |
| FR2075714A5 (en) | 1971-10-08 |
| DE2102368B2 (en) | 1979-05-10 |
| ES387406A1 (en) | 1973-05-01 |
| NL7000812A (en) | 1971-07-23 |
| CA938106A (en) | 1973-12-11 |
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