CN103497773B - Straw carbonization furnace - Google Patents
Straw carbonization furnace Download PDFInfo
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- CN103497773B CN103497773B CN201310453207.XA CN201310453207A CN103497773B CN 103497773 B CN103497773 B CN 103497773B CN 201310453207 A CN201310453207 A CN 201310453207A CN 103497773 B CN103497773 B CN 103497773B
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- water
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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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
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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
- 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
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- Coke Industry (AREA)
- Fire-Extinguishing By Fire Departments, And Fire-Extinguishing Equipment And Control Thereof (AREA)
Abstract
The invention discloses a straw carbonization furnace with high thermal conversion efficiency. The straw carbonization furnace comprises a furnace body, a large furnace door and a small furnace door, wherein the large furnace door and the small furnace door are arranged at one side of the furnace body; the large furnace door is connected with the furnace body through a large furnace door sealing compression bar and a large furnace door hinge; the small furnace door is connected with the large furnace door through a small furnace door sealing compression bar and a small furnace door hinge; the furnace body is internally provided with a combustion chamber; the furnace body surrounding the combustion chamber is provided with a water interlayer; the upper end of the water interlayer is provided with an exhaust port and a water inlet; the upper end of the combustion chamber is provided with a smoke outlet pipe; the lower end of the furnace body is provided with a hot water outlet pipe and a hot water pump which are connected with the water interlayer; the combustion chamber is internally provided with a temperature detecting probe; the furnace body is provided with a control device connected with the temperature detecting probe.
Description
Technical field
The present invention relates to a kind of stalk carbonizing device, particularly relate to a kind of stalk coke oven.
Background technology
China is large agricultural country, and stalk resource is very abundant, for making full use of these resources, replacing coal, electric power, playing its advantage function.At present, domestic straw utilization rate only accounts for about 30%, through technical finesse utilization be also insignificant, most or consumption naturally, crop straw burning phenomenon remains incessant after repeated prohibition, contaminate environment, brings serious harm to the physical and mental health of people.In order to allow peasant, remaining straw collecting is carried out charing people and have developed stalk coke oven, burning charing is carried out to stalk, existing stalk coke oven, thermal transition efficiency is low, waste-gas cleaning effect is bad, can not realize smoke dust discharge, not meet environment protection standard, running cost is higher, and current consumption is larger.
Summary of the invention
Technical problem to be solved by this invention is: provide the stalk coke oven that a kind of thermal transition efficiency is high.
In order to solve the problems of the technologies described above, the technical solution used in the present invention is: stalk coke oven, comprise: body of heater, be arranged on the large fire door of body of heater side and little fire door, described large fire door is connected with body of heater with large firedoor hinge by large oven door sealing depression bar, and described port gate open too small oven door sealing depression bar is connected with large fire door with little firedoor hinge, in described body of heater, be provided with burner hearth, body of heater around described burner hearth is provided with water interlayer, arranges in the upper end of described water interlayer
There are water interlayer venting port and interlayer water-in, the upper end of described burner hearth is provided with pipe, to be connected with water interlayer hot water outlet pipe and hot water pump is provided with in the lower end of described body of heater, described burner hearth inside is provided with temperature measuring probe, described body of heater is provided with the control device be connected with temperature measuring probe.
In order to solve the problems of the technologies described above better, the further technical scheme that the present invention adopts is: on the body of heater of described water interlayer both sides, be respectively arranged with some heat pipes, the two ends of heat pipe are connected with water interlayer respectively.
In order to solve the problems of the technologies described above better, the further technical scheme that the present invention adopts is: the upper end of described body of heater is provided with cooling water tank, the upper end of described cooling water tank is provided with cooling water tank water-in, the lower end of described cooling water tank is provided with cooling water tank rising pipe and splitter, described splitter is by being connected with charing vacuum primingpump by the first connecting water pipe, and described charing vacuum primingpump is connected with charcoal cooling spray by the second connecting water pipe.
In order to solve the problems of the technologies described above better, the further technical scheme that the present invention adopts is: on described body of heater, be provided with foam cleaning apparatus, the structure of described foam cleaning apparatus comprises: the foam dedusting spray chamber be connected with described pipe, be arranged on the one-time dedusting water tank of foam dedusting spray chamber lower end on body of heater, it is indoor that described one-time dedusting water tank is supported on described foam dedusting atomization by some back up pads, described foam dedusting spray chamber is provided with high-pressure atomization shower nozzle, described high-pressure atomization shower nozzle is connected with the high-pressure pump be fixedly installed on described body of heater by the 3rd connecting water pipe, described high-pressure pump is connected with described splitter by the 4th connecting water pipe, the described foam dedusting spray chamber the other end connects flue by first and is connected with the inside of the final dusting water tank be arranged on body of heater, some dedusting baffle plates are provided with in described final dusting water tank, the upper end of described final dusting water tank connects flue by second and is connected with blower fan, described blower fan connects flue by the 3rd and is connected with the inside of the third dedusting water tank be arranged on body of heater, described third dedusting water tank is connected with escape pipe, attached water tank is connected with in the outside of described final dusting water tank, water level pipe and blow-off pipe is provided with in described attached water tank, described one-time dedusting water tank is connected by the 5th connecting water pipe with between third dedusting water tank, described third dedusting water tank is connected by the first water outlet with between final dusting water tank, described final dusting water tank is connected by the second water outlet with between attached water tank.
In order to solve the problems of the technologies described above better, the further technical scheme that the present invention adopts is: on described water level pipe, be connected with the first wastewater treatment case and the second wastewater treatment case, in described first wastewater treatment case, be provided with gac, in described second wastewater treatment case, be provided with filtering net and gac.
In order to solve the problems of the technologies described above better, the further technical scheme that the present invention adopts is: be provided with two cooling water tanks in the upper end of described body of heater, is connected between two cooling water tanks by the 6th connecting water pipe.
In order to solve the problems of the technologies described above better, the further technical scheme that the present invention adopts is: be also provided with large water tank interconnective with water interlayer upper end in the upper end of described body of heater, described water interlayer venting port and interlayer water-in are arranged on the upper end of large water tank.
In order to solve the problems of the technologies described above better, the further technical scheme that the present invention adopts is: in described large fire door, be also provided with water interlayer, in large fire door, the upper end of water interlayer is connected with described splitter by the 7th connecting water pipe, the fire door interlayer venting port be connected with water interlayer in large fire door is provided with in the upper end of described large fire door, the water port be connected with water interlayer in large fire door is provided with in the lower end of described large fire door, described large fire door is provided with the domestic water water outlet be connected with water interlayer in large fire door, body of heater below described domestic water water outlet is fixedly installed pallet.
In order to solve the problems of the technologies described above better, the further technical scheme that the present invention adopts is: have smoke outlet water tank in the pipe arranged outside of described body of heater upper end, described smoke outlet water tank is provided with high-pressure nozzle, and described high-pressure nozzle is connected with the charing vacuum primingpump be fixedly installed on described body of heater by the 8th connecting water pipe.
Advantage of the present invention is: above-mentioned stalk coke oven, and thermal transition efficiency is high, can realize stalk and recycle, waste-gas cleaning is effective, can realize smoke dust discharge, meet environment protection standard, stalk fuel is in liberal supply, and floor space is little, easy for installation, simple to operate, for ease of maintenaince, whole system without air pressure, equipment operating safety, running cost is low, and current consumption is little.
Accompanying drawing explanation
Fig. 1 is the structural representation of stalk coke oven of the present invention.
Fig. 2 is the backsight structural representation of Fig. 1.
Fig. 3 is the left TV structure schematic diagram of Fig. 1.
Fig. 4 is the plan structure schematic diagram at stalk coke oven top of the present invention.
Fig. 5 is the syndeton schematic diagram of foam cleaning apparatus in stalk coke oven of the present invention.
In figure: 1, body of heater, 2, large fire door, 3, little fire door, 4, large oven door sealing depression bar, 5, large firedoor hinge, 6, little oven door sealing depression bar, 7, little firedoor hinge, 8, burner hearth, 9, water interlayer, 10, water interlayer venting port, 11, interlayer water-in, 12, pipe, 13, hot water outlet pipe, 14, hot water pump, 15, temperature measuring probe, 16, control device, 17, heat pipe, 18, cooling water tank, 19, cooling water tank water-in, 20, cooling water tank rising pipe, 21, splitter, 22, first connecting water pipe, 23, charing vacuum primingpump, 24, second connecting water pipe, 25, charcoal cooling spray, 26, foam dedusting spray chamber, 27, one-time dedusting water tank, 28, back up pad, 29, high-pressure atomization shower nozzle, 30, 3rd connecting water pipe, 31, high-pressure pump, 32, 4th connecting water pipe, 33, first connects flue, 34, final dusting water tank, 35, dedusting baffle plate, 36, second connects flue, 37, blower fan, 38, 3rd connects flue, 39, third dedusting water tank, 40, escape pipe, 41, attached water tank, 42, water level pipe, 43, blow-off pipe, 44, 5th connecting water pipe, 45, first water outlet, 46, second water outlet, 47, first wastewater treatment case, 48, second wastewater treatment case, 49, filtering net, 50, 6th connecting water pipe, 51, large water tank, 52, 7th connecting water pipe, 53, water port, 54, domestic water water outlet, 55, pallet, 56, smoke outlet water tank, 57, high-pressure nozzle, 58, 8th connecting water pipe, 59, fire door interlayer venting port, 60, large oven door sealing depression bar seat, 61, little oven door sealing depression bar seat.
Embodiment
Below in conjunction with the drawings and specific embodiments describe in detail of the present invention concrete in
Hold.
As shown in Figure 1, Figure 2, shown in Fig. 3, Fig. 4, Fig. 5, stalk coke oven, comprise: body of heater 1, be arranged on large fire door 2 and the little fire door 3 of body of heater 1 side, described large fire door 2 is connected with body of heater 1 with large firedoor hinge 5 by large oven door sealing depression bar 4, described little fire door 3 is connected with large fire door 2 with little firedoor hinge 7 by little oven door sealing depression bar 6, burner hearth 8 is provided with in described body of heater 1, body of heater 1 around described burner hearth 8 is provided with water interlayer 9, the upper end of described water interlayer 9 is provided with water interlayer venting port 10 and interlayer water-in 11,
The upper end of described burner hearth 8 is provided with pipe 12, to be connected with water interlayer 9 hot water outlet pipe 13 and hot water pump 14 is provided with in the lower end of described body of heater 1, described burner hearth 8 inside is provided with temperature measuring probe 15, described body of heater 1 is provided with the control device 16 be connected with temperature measuring probe 15.
In order to prevent body of heater 1 to be out of shape, strengthen the intensity protection body of heater 1 of body of heater 1, the body of heater 1 of described water interlayer 9 both sides is respectively arranged with some heat pipes 17, and the two ends of heat pipe 17 are connected with water interlayer 9 respectively.
Charcoal naked light during in order to prevent out charcoal, spraying cooling is carried out when charcoal is gone out to charcoal, the upper end of described body of heater 1 is provided with cooling water tank 18, the upper end of described cooling water tank 18 is provided with cooling water tank water-in 19, the lower end of described cooling water tank 18 is provided with cooling water tank rising pipe 20 and splitter 21, described splitter 21 is by being connected with charing vacuum primingpump 23 by the first connecting water pipe 22, and described charing vacuum primingpump 23 is connected with charcoal cooling spray 25 by the second connecting water pipe 24.
In order to the flue gas discharged straw burning carries out dedusting, make it discharge and meet environmental requirement, described body of heater 1 is provided with foam cleaning apparatus, the structure of described foam cleaning apparatus comprises: the foam dedusting spray chamber 26 be connected with described pipe 12, be arranged on the one-time dedusting water tank 27 of foam dedusting spray chamber 26 lower end on body of heater 1, described one-time dedusting water tank 27 is supported in described foam dedusting spray chamber 26 by some back up pads 28, described foam dedusting spray chamber 26 is provided with high-pressure atomization shower nozzle 29, described high-pressure atomization shower nozzle 29 is connected with the high-pressure pump 31 be fixedly installed on described body of heater 1 by the 3rd connecting water pipe 30
Connect, described high-pressure pump 31 is connected with described splitter 21 by the 4th connecting water pipe 32
Connect, described foam dedusting spray chamber 26 the other end connects flue 33 by first and is connected with the inside of the final dusting water tank 34 be arranged on body of heater 1, some dedusting baffle plates 35 are provided with in described final dusting water tank 34, the upper end of described final dusting water tank 34 connects flue 36 by second and is connected with blower fan 37, described blower fan 37 connects flue 38 by the 3rd and is connected with the inside of the third dedusting water tank 39 be arranged on body of heater 1, described third dedusting water tank 39 is connected with escape pipe 40, attached water tank 41 is connected with in the outside of described final dusting water tank 34, water level pipe 42 and blow-off pipe 43 is provided with in described attached water tank 41, described one-time dedusting water tank 27 is connected by the 5th connecting water pipe 44 with between third dedusting water tank 39, described third dedusting water tank 39 is connected by the first water outlet 45 with between final dusting water tank 34, be connected by the second water outlet 46 between described final dusting water tank 34 with attached water tank 41.
In order to the sewage of discharging water level pipe 42 processes, make it discharge and meet environmental requirement, decreasing pollution, described water level pipe 42 is connected with the first wastewater treatment case 47 and the second wastewater treatment case 48, in described first wastewater treatment case 47, be provided with gac, in described second wastewater treatment case 48, be provided with filtering net 49 and gac.
In order to make stalk coke oven one-piece construction more reasonable, practical, being provided with in the upper end of described body of heater 1 between two cooling water tanks 18, two cooling water tank 18 and being connected by the 6th connecting water pipe 50.
In order to make stalk coke oven one-piece construction more reasonable, improve heating efficiency, also be provided with large water tank 51 interconnective with water interlayer 9 upper end in the upper end of described body of heater 1, described water interlayer venting port 10 and interlayer water-in 11 are arranged on the upper end of large water tank 51.
In order to make, heat is more high efficiency to be utilized, hot water for life is provided, also water interlayer is provided with in described large fire door 2, in large fire door 2, the upper end of water interlayer is connected with described splitter 21 by the 7th connecting water pipe 52, the fire door interlayer venting port 59 be connected with water interlayer in large fire door 2 is provided with in the upper end of described large fire door 2, the water port 53 be connected with water interlayer in large fire door 2 is provided with in the lower end of described large fire door 2, described large fire door 2 is provided with the domestic water water outlet 54 be connected with water interlayer in large fire door 2, body of heater 1 below described domestic water water outlet 16 is fixedly installed pallet 55.
In order to reduce the temperature of smoke outlet, heat is made to obtain more high efficiency utilization, smoke outlet water tank 56 is had in pipe 12 arranged outside of described body of heater 1 upper end, described smoke outlet water tank 56 is provided with high-pressure nozzle 57, and described high-pressure nozzle 57 is connected with the charing vacuum primingpump 23 be fixedly installed on described body of heater 1 by the 8th connecting water pipe 58.
When above-mentioned stalk coke oven uses, by interlayer water-in 11 to large water tank 51 and water interlayer 9 water filling, by cooling water tank water-in 19 to water filling in cooling water tank 18, the water in cooling water tank 18 to enter in large fire door 2 in water interlayer by cooling water tank rising pipe 20, splitter 21, the 7th connecting water pipe 52.
By rotating large oven door sealing depression bar 4, the large oven door sealing depression bar seat 60 on itself and body of heater 1 is separated from each other, thus large fire door 2 is opened carry out stalk fuel interpolation, also can according to use needs, by rotating little oven door sealing depression bar 6, the little oven door sealing depression bar seat 61 on itself and body of heater 1 is separated from each other, thus little fire door 3 is opened, carry out stalk fuel interpolation by little fire door 3.
Straw burning in burner hearth 8 produces heat to the water interlayer 9 of burner hearth 8 surrounding and large fire door
In 2, water interlayer heats, the temperature in burner hearth 8 is detected by control device 16 control temperature detection probe 15, hot water in water interlayer 9 can pump use by hot water outlet pipe 13 and hot water pump 14, and in large fire door 2, the hot water of water interlayer can be released by domestic water water outlet 54 and be used.
The flue gas produced during burning is discharged by pipe 12, smoke outlet water tank 56 is had in pipe 12 arranged outside of described body of heater 1 upper end, smoke outlet water tank 56 can reduce the temperature of smoke outlet, make heat obtain more high efficiency utilization, the water of smoke outlet water tank 56 is through: the water in cooling water tank 18 is provided by cooling water tank rising pipe 20, splitter 21, first connecting water pipe 22, charing vacuum primingpump 23, the 8th connecting water pipe 58 and high-pressure nozzle 57.Flue gas in pipe 12 enters foam dedusting spray chamber 26, high-pressure atomization shower nozzle 29 sprays the flue gas entered, water in high-pressure atomization shower nozzle 29 is through, and the water in cooling water tank 18 is provided by cooling water tank rising pipe 20, splitter 21, the 4th connecting water pipe 32, high-pressure pump 31, the 3rd connecting water pipe 30.Water after spray is discharged by described one-time dedusting water tank 27, the 5th connecting water pipe 44, third dedusting water tank 39, first water outlet 45, final dusting water tank 34, second water outlet 46, attached water tank 41 and water level pipe 42, and water level pipe 42 is discharged and directly discharged after the first wastewater treatment case 47 and the second wastewater treatment case 48 filter.Flue gas after the dedusting of foam dedusting spray chamber 26 connects flue 33 by first and enters final dusting water tank 34 after dedusting baffle plate 35 dedusting, under the effect of blower fan 37 by second connecting flue 36, blower fan 37, the 3rd is discharged by escape pipe 40 after connecting third dedusting water tank 39 dedusting that enters of flue 38.
Above-mentioned stalk coke oven can be used for processing agricultural crop straw, solves straw from village burning and asks
Topic, normalization process is carried out to agricultural crop straw, peasant is allowed to be carbonized by remaining straw collecting, utilize the waste that agriculture production goes out, as: cotton, soybean, corn, Chinese sorghum, castor-oil plant, Sunflower Receptacle, sesame, eggplant, tomato, capsicum, branch in the patterns such as tobacco leaf and forestry, sawdust, raw material made by sawdust, can direct production charcoal, energy reaches 5500-6500 kilocalorie, every platform equipment hot water 8-10 ton supplying 80 degree of-100 degree per hour, consume fuel about 600 jin, water temperature is self controllable, this equipment sustainable supply hot water, be applicable to bath center hot water service, enterprises and institutions' hot water service, also can be used for water heating air supply, be applicable to urban cells, group of enterprises, the domestic water of ecological park, heating etc., can according to the product of different customer requirement customization different size, heat energy is plain cylindrical furnace 5-6 times, energy consumption lower than 3-4 doubly.
Claims (6)
1. stalk coke oven, it is characterized in that: comprising: body of heater (1), be arranged on large fire door (2) and the little fire door (3) of body of heater (1) side, described large fire door (2) is connected with body of heater (1) with large firedoor hinge (5) by large oven door sealing depression bar (4), described little fire door (3) is connected with large fire door (2) with little firedoor hinge (7) by little oven door sealing depression bar (6), burner hearth (8) is provided with in described body of heater (1), body of heater (1) around described burner hearth (8) is provided with water interlayer (9), water interlayer venting port (10) and interlayer water-in (11) is provided with in the upper end of described water interlayer (9), the upper end of described burner hearth (8) is provided with pipe (12), to be connected with water interlayer (9) hot water outlet pipe (13) and hot water pump (14) is provided with in the lower end of described body of heater (1), described burner hearth (8) inside is provided with temperature measuring probe (15), described body of heater (1) is provided with the control device (16) be connected with temperature measuring probe (15), the body of heater (1) of described water interlayer (9) both sides is respectively arranged with some heat pipes (17), and the two ends of heat pipe (17) are connected with water interlayer (9) respectively, the upper end of described body of heater (1) is provided with cooling water tank (18), the upper end of described cooling water tank (18) is provided with cooling water tank water-in (19), cooling water tank rising pipe (20) and splitter (21) is provided with in the lower end of described cooling water tank (18), described splitter (21) is connected with charing vacuum primingpump (23) by the first connecting water pipe (22), and described charing vacuum primingpump (23) is connected with charcoal cooling spray (25) by the second connecting water pipe (24), described body of heater (1) is provided with foam cleaning apparatus, the structure of described foam cleaning apparatus comprises: the foam dedusting spray chamber (26) be connected with described pipe (12), be arranged on the one-time dedusting water tank (27) of upper foam dedusting spray chamber (26) lower end of body of heater (1), described one-time dedusting water tank (27) is supported in described foam dedusting spray chamber (26) by some back up pads (28), described foam dedusting spray chamber (26) is provided with high-pressure atomization shower nozzle (29), described high-pressure atomization shower nozzle (29) is connected with the high-pressure pump (31) be fixedly installed on described body of heater (1) by the 3rd connecting water pipe (30), described high-pressure pump (31) is connected with described splitter (21) by the 4th connecting water pipe (32), described foam dedusting spray chamber (26) the other end connects flue (33) by first and is connected with the inside of the final dusting water tank (34) be arranged on body of heater (1), some dedusting baffle plates (35) are provided with in described final dusting water tank (34), the upper end of described final dusting water tank (34) connects flue (36) by second and is connected with blower fan (37), described blower fan (37) connects flue (38) by the 3rd and is connected with the inside of the third dedusting water tank (39) be arranged on body of heater (1), described third dedusting water tank (39) is connected with escape pipe (40), attached water tank (41) is connected with in the outside of described final dusting water tank (34), water level pipe (42) and blow-off pipe (43) is provided with in described attached water tank (41), described one-time dedusting water tank (27) is connected by the 5th connecting water pipe (44) with between third dedusting water tank (39), described third dedusting water tank (39) is connected by the first water outlet (45) with between final dusting water tank (34), described final dusting water tank (34) is connected by the second water outlet (46) with between attached water tank (41).
2.
2according to the stalk coke oven that claim 1 is stated, it is characterized in that: on described water level pipe (42), be connected with the first wastewater treatment case (47) and the second wastewater treatment case (48), in described first wastewater treatment case (47), be provided with gac, in described second wastewater treatment case (48), be provided with filtering net (49) and gac.
3.
according to the stalk coke oven that claim 2 is stated, it is characterized in that: be provided with two cooling water tanks (18) in the upper end of described body of heater (1), connected by the 6th connecting water pipe (50) between two cooling water tanks (18).
4.
according to the stalk coke oven that claim 3 is stated, it is characterized in that: be also provided with and the interconnective large water tank in water interlayer (9) upper end (51) in the upper end of described body of heater (1), described water interlayer venting port (10) and interlayer water-in (11) are arranged on the upper end of large water tank (51).
5.
5according to the stalk coke oven that claim 4 is stated, it is characterized in that: in described large fire door (2), be also provided with water interlayer, the upper end of large fire door (2) interior water interlayer is connected with described splitter (21) by the 7th connecting water pipe (52), the fire door interlayer venting port (59) be connected with water interlayer in large fire door (2) is provided with in the upper end of described large fire door (2), the water port (53) be connected with water interlayer in large fire door (2) is provided with in the lower end of described large fire door (2), described large fire door (2) is provided with the domestic water water outlet (54) be connected with water interlayer in large fire door (2), the body of heater (1) of described domestic water water outlet (16) below is fixedly installed pallet (55).
6.
6according to the stalk coke oven that claim 5 is stated, it is characterized in that: have smoke outlet water tank (56) in pipe (12) arranged outside of described body of heater (1) upper end, described smoke outlet water tank (56) is provided with high-pressure nozzle (57), and described high-pressure nozzle (57) is connected with the charing vacuum primingpump (23) be fixedly installed on described body of heater (1) by the 8th connecting water pipe (58).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310453207.XA CN103497773B (en) | 2013-09-29 | 2013-09-29 | Straw carbonization furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310453207.XA CN103497773B (en) | 2013-09-29 | 2013-09-29 | Straw carbonization furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103497773A CN103497773A (en) | 2014-01-08 |
| CN103497773B true CN103497773B (en) | 2015-02-25 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310453207.XA Expired - Fee Related CN103497773B (en) | 2013-09-29 | 2013-09-29 | Straw carbonization furnace |
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| CN (1) | CN103497773B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111621306B (en) * | 2020-05-25 | 2021-12-14 | 西伯瀚(泰兴)传动技术有限公司 | Vertical carbonization furnace for gas coal coking |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN200972242Y (en) * | 2006-08-07 | 2007-11-07 | 李志辉 | Energy-saving boiler |
| CN101555412A (en) * | 2008-04-11 | 2009-10-14 | 周永宏 | Straw carbonization furnace |
| CN202835772U (en) * | 2011-11-24 | 2013-03-27 | 孙健 | Highly-efficient energy-saving green boiler burning straw briquette coal |
| CN103013536A (en) * | 2011-09-21 | 2013-04-03 | 冯益忠 | Environment-friendly straw carbonization furnace |
| CN203533870U (en) * | 2013-09-29 | 2014-04-09 | 盐城市诚鑫机械制造有限公司 | Straw carbonization water heating furnace |
| CN203530226U (en) * | 2013-09-29 | 2014-04-09 | 盐城市诚鑫机械制造有限公司 | Straw charring furnace |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001164259A (en) * | 1999-12-08 | 2001-06-19 | Shinagawa Refract Co Ltd | Quenching box for carbonization furnace |
| JP2012077231A (en) * | 2010-10-05 | 2012-04-19 | Takeo Hirahara | Easy and inexpensive movable simple carbonization furnace |
-
2013
- 2013-09-29 CN CN201310453207.XA patent/CN103497773B/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN200972242Y (en) * | 2006-08-07 | 2007-11-07 | 李志辉 | Energy-saving boiler |
| CN101555412A (en) * | 2008-04-11 | 2009-10-14 | 周永宏 | Straw carbonization furnace |
| CN103013536A (en) * | 2011-09-21 | 2013-04-03 | 冯益忠 | Environment-friendly straw carbonization furnace |
| CN202835772U (en) * | 2011-11-24 | 2013-03-27 | 孙健 | Highly-efficient energy-saving green boiler burning straw briquette coal |
| CN203533870U (en) * | 2013-09-29 | 2014-04-09 | 盐城市诚鑫机械制造有限公司 | Straw carbonization water heating furnace |
| CN203530226U (en) * | 2013-09-29 | 2014-04-09 | 盐城市诚鑫机械制造有限公司 | Straw charring furnace |
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| CN103497773A (en) | 2014-01-08 |
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