CN103542524A - Condensation horizontal water jacket heating furnace - Google Patents
Condensation horizontal water jacket heating furnace Download PDFInfo
- Publication number
- CN103542524A CN103542524A CN201210241466.1A CN201210241466A CN103542524A CN 103542524 A CN103542524 A CN 103542524A CN 201210241466 A CN201210241466 A CN 201210241466A CN 103542524 A CN103542524 A CN 103542524A
- Authority
- CN
- China
- Prior art keywords
- smoke box
- heat
- pipe
- flue gas
- smoke
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- 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.)
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 55
- 238000010438 heat treatment Methods 0.000 title claims abstract description 22
- 238000009833 condensation Methods 0.000 title claims abstract description 16
- 230000005494 condensation Effects 0.000 title claims abstract description 16
- 239000000779 smoke Substances 0.000 claims abstract description 48
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 23
- 239000003546 flue gas Substances 0.000 claims abstract description 23
- 239000002918 waste heat Substances 0.000 claims abstract description 6
- 239000007788 liquid Substances 0.000 claims description 9
- 238000012856 packing Methods 0.000 claims description 9
- 230000008030 elimination Effects 0.000 claims description 7
- 238000003379 elimination reaction Methods 0.000 claims description 7
- 230000005855 radiation Effects 0.000 claims description 4
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 claims description 3
- 239000011248 coating agent Substances 0.000 claims description 3
- 238000000576 coating method Methods 0.000 claims description 3
- 238000011049 filling Methods 0.000 claims description 3
- 239000003063 flame retardant Substances 0.000 claims description 3
- 239000008236 heating water Substances 0.000 claims description 3
- 230000007797 corrosion Effects 0.000 abstract description 7
- 238000005260 corrosion Methods 0.000 abstract description 7
- 238000012423 maintenance Methods 0.000 abstract description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 11
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 6
- 239000003345 natural gas Substances 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- 239000003517 fume Substances 0.000 description 2
- 238000007726 management method Methods 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 238000002679 ablation Methods 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000006056 electrooxidation reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 230000035807 sensation Effects 0.000 description 1
- 238000012549 training Methods 0.000 description 1
- 238000001291 vacuum drying Methods 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
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Classifications
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- 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
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Details Of Fluid Heaters (AREA)
Abstract
The invention discloses a condensation horizontal water jacket heating furnace, which is designed for the purposes of prolonging the service life of the heating furnace and improving the thermal efficiency of the heating furnace, and mainly comprises a cylinder body, a front panel, a rear tube plate and a rear panel, a front smoke box and a condensate water discharge unit, a heat pipe condenser, a heat exchange tube disc, a temperature sensor, a combined furnace liner, a rear smoke box, a convection smoke tube and the like, wherein the cylinder body is connected with the front tube plate, the front panel, the rear tube plate and the rear panel, the front smoke box and the condensate water discharge unit are arranged between the front tube plate and the front panel, the heat pipe condenser is arranged in the front smoke. The high-temperature flue gas enters the combined furnace pipe to release heat and then is collected by the smoke box, and returns to the front smoke box through the convection smoke pipe, and the flue gas waste heat is discharged by the chimney after being subjected to heat exchange by the heat pipe condenser to the heated medium in the cylinder. The heating furnace can fully utilize the steam potential and the flue gas waste heat in the flue gas, reduce the temperature of the flue gas to 110 ℃, improve the heat efficiency by 93 percent, effectively solve the problems of dew point corrosion and the discharge of condensed water on the heating surface at the tail part of the heating furnace, and has the advantages of compact furnace body structure, reasonable component layout and convenient manufacture, maintenance and repair.
Description
Technical field
The present invention relates to the horizontal water batch heater of a kind of condensation, belong to oil field special heating furnace technical field.
Background technology
Station in oilfield special heating furnace mainly adopts vertical and horizontal two kinds, mainly undertake the heat supply task of oil gas field, be one of consumable fuel apparatus of oil gas field maximum, the height of its technical merit and the thermal efficiency directly affects technical merit, energy-saving and emission-reduction and the economic benefit that oil-gas field surface engineering is built.In recent years, water batch heater is widely used in oilfield surface engineering with its reliable security performance.But water batch heater is limited by dew-point temperature generally, high fume temperature, energy in flue gas and steam latent heat can not be used effectively (vacuum drying oven and tubular heater also exist problems), cause that the water batch heater thermal efficiency is low, the problem such as energy waste and environmental thermal pollution.
Mainly there is following problem in the water batch heater in application:
One. the efficiency of heating surface is not high: although the design stove of heating furnace is imitated generally in 90% left and right, the actual motion thermal efficiency of the most of water jacket furnace in oil field is not high, and principal element has following several respects:
1. the heat convection of water jacket furnace self structure defective effect flue gas and smoke pipe, also affects the heat exchange of heated medium and heat(ing) coil, thereby reduces the thermal efficiency;
2. due to water jacket furnace, be subject to the restriction of flue gas dew point temperature, cause exhaust gas temperature higher (other heating furnace also exists this problem), the efficient heat in flue gas can not make full use of, thereby reduces the thermal efficiency;
3. water jacket furnace self combustor efficiency is not high.Conventional negative-pressure ejecting scroll casing type burner stove tank flame temperature is not high, and radiation intensity is low, reduces efficiency of combustion;
4. water jacket furnace insulation is bad, and operational management is not in place, reduces heater efficiency.
Two. water jacket furnace surplus and air coefficient are bigger than normal:
Because burner type selecting is improper, the water jacket furnace of on-the-spot operation is superfluous, and air coefficient major part is higher, how 2.0～3.0 operations, does not reach optimum value.Best excess air coefficient should be controlled by different combustion systems, for should being controlled between 1.05～1.20 of pressurized firing, for should being controlled between 1.4～2.0 of gravity-flow ventilation burning.
Three. the perishable perforation of water jacket furnace causes leakage, and service life is shorter:
The weld seam at smoke-fire-tube and burner hearth connecting bend place occurs to leak the corrosion that causes water jacket furnace, and one of reason is the corrosion that the condensation water in natural gas causes, the personal temperature degree of water jacket furnace is not high, and the easy condensation of saturated steam in natural gas becomes aqueous water, is ionized into H
+and OH
-.H
+with natural gas, H
2product C O after S burning
2and SO
2generate respectively H
2cO
3and H
2sO
3, under HTHP, aggravated the corrosion of pyrotechnics pipeline and weld seam.Former two is therefore that water jacket furnace adopts " U " structure, and the commissure that pyrotechnics system easily connects tube sheet place at smoke pipe, front and back tube sheet and smoke pipe corrosion failure occurs and leaks, the electrochemical corrosion that also has the condensation water that produces after right gas firing to cause.
Four. the metering of water jacket furnace is generally not up to standard:
Owing to can gratuitously using associated gas in Oil and gas station, for saving the fund of building of producing, heating furnace is not all implemented separate unit combustion gas and quantity of heat given up metering in accordance with regulations, causes the gas consumption that cannot accurately obtain water jacket furnace.
Five. there is weak link in water jacket furnace operation operational management:
Do not set up the judgement start and stop method of a set of science,, according to determine the start and stop of stove in station by the relativeness of medium temperature in hot factor and stove, only often do not open ahead of time stove or time delay blowing out with sensation by rule of thumb, extended the running time of stove, cause energy waste.The technical skill training of shortage to employee, does not form regular maintenance system.In the long-time water batch heater using, burner and the blocking water corrosion phenomena of sealing up a door is general, the phenomenons such as internal structure obstruction, gas nozzle ablation and induction tunnel damage occur often, the anhydrous gentle exhaust gas temperature meter of water batch heater or temperature reading distortion, water blind roaster level gauge indication is unintelligible, smoke-fire-tube fouling.
Summary of the invention
The object of the present invention is to provide the horizontal water batch heater of a kind of condensation, its service life is longer, and good manufacturability can make full use of steam potential and waste heat in flue gas, and energy utilization rate is high.
Concrete technical scheme of the present invention is as follows:
Water batch heater horizontal cylinder is connected front tube sheet and front panel by upper connecting rod with lower link front end, and rear end is connected with back tube sheet and the rear board of heating delivery port.
Between front tube sheet and front panel, be provided with semicircular and have the front smoke box of both sides extension pipe, heat pipe condenser two ends are located at respectively in front smoke box and cylindrical shell.Heat pipe condenser below is provided with the condensed water elimination unit being comprised of aqueduct, liquid packing and drainpipe, aqueduct one end connects front smoke box extension pipe, the other end is connected with the liquid packing of rectilinear dividing plate, and the liquid packing other end connects drainpipe, and two-way drainpipe collects rear connection outlet.
Cylindrical shell internal upper part is provided with upper and lower two-layer coiled heat exchanger tube Pan， lower floor heat exchanger tube dish and is greater than upper strata heat exchanger tube dish.In cylindrical shell, middle part is provided with temperature sensor, and bottom is provided with the combination flue by flue stent support, and combination flue front end is provided with flame retardant coating, and rear end is connected with the rear smoke box of antibomb unit, and rear smoke box and front smoke box are communicated with by the convection current smoke pipe of combination flue both sides.
Cylindrical shell top is provided with hanger, filling pipe, manhole, base and atmospheric communicating pipe, and cylinder body bottom is provided with saddle, blow-off pipe and heating water inlet.
The operation principle of heating furnace of the present invention is as follows:
When the horizontal water jacket furnaceman of this condensation is done, first the high-temperature flue gas that burner produces enters combination flue radiation heat release, flue gas after heat release enters rear smoke box and collects and by convection current smoke pipe, get back to front smoke box again, by heat pipe condenser heat exchange, waste heat is passed to after the heated medium in cylindrical shell by smoke stack emission.Low-temperature flue gas and heat pipe condenser change thermogenetic condensate water and collect in front smoke box bottom, by condensed water elimination unit safety dumping.
Heating furnace of the present invention can make full use of steam potential and the fume afterheat in flue gas, and exhaust gas temperature is down to 110 ℃, improves the thermal efficiency and reaches 93%.Heating furnace body compact conformation, assembly layout is reasonable, is convenient to manufacture and maintaining.By the design of condensing unit and seal drain, can effectively solve the emission problem of dew point corrosion and heating furnace back-end surfaces condensed water.
Accompanying drawing explanation
Fig. 1 is the horizontal water jacket heating furnace structure of condensation schematic diagram.
Fig. 2 is the horizontal water batch heater A-A of condensation cutaway view.
Fig. 3 is the horizontal water batch heater heat exchanger tube of condensation dish schematic diagram.
Fig. 4 is the horizontal water batch heater front smoke box of condensation and condensed water elimination cell schematics.
The specific embodiment
Referring to figs. 1 through 4 pairs of embodiments of the invention, further illustrate:
Embodiment:
Water batch heater horizontal cylinder 2 is connected front tube sheet 10 and front panel 6 by upper connecting rod 19 with lower link 21 front ends, and rear end is connected with back tube sheet 16 and the rear board 20 of heating delivery port 17.
Between front tube sheet 10 and front panel 6, be provided with semicircular and have the front smoke box 8 of both sides extension pipe, heat pipe condenser 7 two ends are located at respectively in front smoke box 8 and cylindrical shell 2.Heat pipe condenser 7 belows are provided with the condensed water elimination unit 4 being comprised of aqueduct 41, liquid packing 42 and drainpipe 44, aqueduct 41 one end connect front smoke box 8 extension pipes, the other end is connected with the liquid packing 42 of rectilinear dividing plate 43, liquid packing 42 other ends connect drainpipe 44, and two-way drainpipe 44 collects rear connection outlet 45.
During work, first the high-temperature flue gas that burner produces enters the 3 radiation heat releases of combination flue, flue gas after heat release enters rear smoke box 23 and collects, flue gas after collection is got back to front smoke box 8 by convection current smoke pipe 27 convection heat transfer' heat-transfer by convection again, then, low-temperature flue gas, through heat pipe condenser 7 condensing heat-exchanges, is passed to the heated medium in cylindrical shell 2 by waste heat, finally by smoke stack emission.Meanwhile, low-temperature flue gas changes thermogenetic flue gas condensed at heat pipe condenser 7 and bears water the bottom that collects in front smoke box 8, by condensed water elimination unit 4 safety dumpings.
Claims (2)
1. the horizontal water batch heater of condensation, is characterized in that:
Water batch heater horizontal cylinder (2) is connected front tube sheet (10) and front panel (6) by upper connecting rod (19) with lower link (21) front end, and rear end is connected with back tube sheet (16) and the rear board (20) of heating delivery port (17);
Between front tube sheet (10) and front panel (6), be provided with semicircular and have the front smoke box (8) of both sides extension pipe, heat pipe condenser (7) two ends are located at respectively in front smoke box (8) and cylindrical shell (2); Heat pipe condenser (7) below is provided with the condensed water elimination unit (4) being comprised of aqueduct (41), liquid packing (42) and drainpipe (44), aqueduct (41) one end connects front smoke box (8) extension pipe, the other end is connected with the liquid packing (42) of rectilinear dividing plate (43), liquid packing (42) other end connects drainpipe (44), and two-way drainpipe (44) collects rear connection outlet (45);
Cylindrical shell (2) internal upper part is provided with upper and lower two-layer coiled heat exchanger tube dish (18), and lower floor's heat exchanger tube dish is greater than upper strata heat exchanger tube dish; In cylindrical shell (2), middle part is provided with temperature sensor (9), bottom is provided with the combination flue (3) being supported by flue support (25), combination flue (3) front end is provided with flame retardant coating (5), rear end is connected with the rear smoke box (23) of antibomb unit (22), and rear smoke box (23) and front smoke box (8) are communicated with by the convection current smoke pipe (27) of combination flue (3) both sides;
Cylindrical shell (2) top is provided with hanger (11), filling pipe (12), manhole (13), base (14) and atmospheric communicating pipe (15), and cylindrical shell (2) bottom is provided with saddle (1), blow-off pipe (24) and heating water inlet (26).
2. the horizontal water batch heater of condensation as claimed in claim 1, it is characterized in that first the high-temperature flue gas that the horizontal water jacket burner for heating furnace of this condensation produces enters the radiation heat release of combination flue (3), flue gas after heat release enters rear smoke box (23) and collects and by convection current smoke pipe (27), get back to front smoke box (8) again, by heat pipe condenser (7) heat exchange, waste heat is passed to after the heated medium in cylindrical shell (2) by smoke stack emission; Low-temperature flue gas and heat pipe condenser (7) change thermogenetic condensate water and collect in front smoke box (8) bottom, by condensed water elimination unit (4) safety dumping.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210241466.1A CN103542524B (en) | 2012-07-12 | 2012-07-12 | Condensation horizontal water jacket heating furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210241466.1A CN103542524B (en) | 2012-07-12 | 2012-07-12 | Condensation horizontal water jacket heating furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103542524A true CN103542524A (en) | 2014-01-29 |
| CN103542524B CN103542524B (en) | 2016-04-06 |
Family
ID=49966235
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201210241466.1A Active CN103542524B (en) | 2012-07-12 | 2012-07-12 | Condensation horizontal water jacket heating furnace |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103542524B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105091338A (en) * | 2014-05-08 | 2015-11-25 | 李明明 | Horizontal condensation type briquette coal heating stove |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0870996A2 (en) * | 1997-04-10 | 1998-10-14 | Gerhard Dr. Luther | Smoke gas converter |
| CN2434613Y (en) * | 2000-07-11 | 2001-06-13 | 上海天行机电设备成套公司 | Condensation heat exchanger appts. |
| CN101162108A (en) * | 2007-11-15 | 2008-04-16 | 于希敏 | Compound gas superconductive heater |
| CN201047670Y (en) * | 2007-06-01 | 2008-04-16 | 青岛青义锅炉有限公司 | Vacuum phase transition boiler |
| CN201522104U (en) * | 2009-09-28 | 2010-07-07 | 裴光泰 | Condensing built-in heat exchanging no-pressure boiler |
| CN202747617U (en) * | 2012-07-12 | 2013-02-20 | 中国石油天然气股份有限公司 | Condensation horizontal water jacket heating furnace |
-
2012
- 2012-07-12 CN CN201210241466.1A patent/CN103542524B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0870996A2 (en) * | 1997-04-10 | 1998-10-14 | Gerhard Dr. Luther | Smoke gas converter |
| CN2434613Y (en) * | 2000-07-11 | 2001-06-13 | 上海天行机电设备成套公司 | Condensation heat exchanger appts. |
| CN201047670Y (en) * | 2007-06-01 | 2008-04-16 | 青岛青义锅炉有限公司 | Vacuum phase transition boiler |
| CN101162108A (en) * | 2007-11-15 | 2008-04-16 | 于希敏 | Compound gas superconductive heater |
| CN201522104U (en) * | 2009-09-28 | 2010-07-07 | 裴光泰 | Condensing built-in heat exchanging no-pressure boiler |
| CN202747617U (en) * | 2012-07-12 | 2013-02-20 | 中国石油天然气股份有限公司 | Condensation horizontal water jacket heating furnace |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105091338A (en) * | 2014-05-08 | 2015-11-25 | 李明明 | Horizontal condensation type briquette coal heating stove |
| CN105091338B (en) * | 2014-05-08 | 2018-03-23 | 李明明 | Sleeping body condensing molded coal heating stove |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103542524B (en) | 2016-04-06 |
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