CN103242908B - Continuous thermal cycle coal gangue pyrolysis gasification humidifying and tail gas purifying device - Google Patents

Continuous thermal cycle coal gangue pyrolysis gasification humidifying and tail gas purifying device Download PDF

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CN103242908B
CN103242908B CN201310121735.5A CN201310121735A CN103242908B CN 103242908 B CN103242908 B CN 103242908B CN 201310121735 A CN201310121735 A CN 201310121735A CN 103242908 B CN103242908 B CN 103242908B
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gas
combustion
chamber
water
waste gas
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CN103242908A (en
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王新民
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Shanxi Xinli Energy Technology Co Ltd
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Shanxi Xinli Energy Technology Co Ltd
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Abstract

The invention provides a continuous thermal cycle coal gangue pyrolysis gasification humidifying and tail gas purifying device which comprises a coal gangue pyrolysis gasification device, a crude gas guiding device, a furnace coal gangue hot waste gas humidifying dehydrating device, and a tail gas showering purifier, wherein the coal gangue pyrolysis gasification device consists of a coal gangue pyrolysis device and a water gas reaction device; the coal gangue pyrolysis device consists of a pyrolysis gasification chamber, an external gas heating device and an internal gas heating device; the water gas reaction device consists of a material cooling device and a steam generation device; the furnace coal gangue hot waste gas humidifying dehydrating device consists of a water vapor discharge guider and a waste gas heat exchange dehydrator; the tail gas showering purifier consists of a purifying cylinder, an atomized sprinkler, a stainless steel filter screen mesh layer, a tail gas deflector, a water tank, an impounding reservoir and a spray water pump; and raw gas guided from the raw gas guiding device is purified and then burnt, the burnt waste gas is sent to the waste gas heat exchange dehydrator to dehydrate coal gangue aggregates in the furnace, and the dehydrated waste gas is purified and discharged by using the tail gas showering purifier.

Description

Thermal cycling continuous coal gangue pyrolytic gasification damping and exhaust gas cleaner
Technical field
The present invention relates to the continuous coal gangue pyrolytic gasification damping of the technology of coal gangue pyrolytic gasification, particularly thermal cycling and exhaust gas cleaner.
Background technology
Coal gangue---the stone selected from raw coal is the waste residue of coal separating plant, bad process, China has the coal gangue of more than one hundred million tons not utilize every year, and still continues to discharge about 100Mt every year, not only piles up occupation of land, and can also spontaneous combustion polluted air or cause fire, cause serious environmental pollution.
Due to the incoalation of 1 years, carbon, oil, gas material containing 20-30% in coal gangue, wherein oil gas accounted for 11-15%, carbon accounts for 7-15%.Coal gangue pyrolytic gasification, (composition is the compositions such as silicon-dioxide, aluminium sesquioxide, ferric oxide, titanium dioxide, calcium oxide, magnesium oxide, potassium oxide, sodium oxide, Vanadium Pentoxide in FLAKES, manganese oxide, sulphur trioxide to obtain the solid product of oil gas product and 70-80%, the grog of sal refractory materials), there is economic worth, more have social benefit.
The present inventor to the physical property of coal gangue and the research of high-temperature coal pyrolytic gasification technique, innovates a set of brand-new coal gangue high temperature pyrolysis and gasification composite technology and device for a long time.
Summary of the invention
The invention provides thermal cycling continuous coal gangue pyrolytic gasification damping and exhaust gas cleaner, the waste heat of hot waste gas of raw gas in coal gangue pyrolytic gasification after reclaiming clean burning is carried out damping dehydration to the coal gangue pellet entering stokehold by this device, and carries out water to the low temperature waste gas after damping dehydration and wash one's hair the discharge of purification neat and tidy.
Realizing the technical scheme that above-mentioned purpose takes is:
Thermal cycling continuous coal gangue pyrolytic gasification damping and exhaust gas cleaner, mainly comprise coal gangue pyrolysis gasifying device, raw gas take-up gear, as-fired coal spoil hot waste gas damping dewatering unit, tail gas water wash one's hair cleaner, described coal gangue pyrolysis gasifying device mainly comprises coal gangue pyrolysis installation and water-gas reaction device, described coal gangue pyrolysis installation is arranged in the middle part of body of heater, mainly comprise pyrolysis vaporizer, outer gas-operated thermal bath facility, interior gas-operated thermal bath facility, central supported bow formation, described pyrolysis vaporizer forms an annulus by the inside and outside ringwall of fire-resistant thermally conductive material, being centered around pyrolysis vaporizer's exterior wall ring periphery is outer gas-operated thermal bath facility, is interior gas-operated thermal bath facility in ringwall ring in pyrolysis vaporizer, described water-gas reaction device comprises pyrolysis vaporizer, material heat sink, steam generation device, the pyrolysis vaporizer of described pyrolysis vaporizer and coal gangue pyrolysis installation is same room, pyrolysis vaporizer is positioned at central supported bow top, described material heat sink, steam generation device is positioned at central supported bow below, described material heat sink comprises high temperature reduction chamber, low temperature cooling chamber, reduction chamber bridge arch, the top of high temperature reduction chamber communicates with bottom pyrolysis vaporizer, high temperature reduction chamber and low temperature cooling chamber setting up and down, reduction chamber bridge arch is arranged between high temperature reduction chamber and low temperature cooling chamber, described reduction chamber bridge arch comprises bridge bow, steam chest, steam enters siphunculus, bridge bow middle part forms steam chest, the lower openings of steam chest is towards low temperature cooling chamber, steam enters siphunculus and is arranged in bridge bow, steam enters siphunculus one end and leads to steam chest, the other end stretches out outside stove, described steam generation device comprises annular hollow metal box body, steam pockets and drum input tube, drum output tube, annular hollow metal box body is arranged on bottom of furnace body, the inner ring cavity of annular hollow metal box body is connected to the low temperature cooling chamber bottom of material heat sink, the body of heater water bag that opposing seal is used for storage of water is formed in annular hollow metal box body case, body of heater water bag is connected to water inlet pipe and drum input tube, water inlet pipe communicates with water tank, drum input tube and steam pockets are connected, drum output tube and the steam of material heat sink of steam pockets enter the siphunculus the other end and communicate, described raw gas take-up gear comprises raw gas concentration chamber, interior derivation passage, outer derivation passage, derive main channel, derive circuit, described raw gas concentration chamber be arranged on the top of pyrolysis vaporizer and pyrolysis vaporizer integrally formed, in interior derivation channel setting quirk partition wall, interior derivation feeder connection leads to pyrolysis vaporizer through in the middle part of interior ringwall, interior derivation channel outlet leads to the raw gas concentration chamber at pyrolysis vaporizer top through interior ringwall, in the exterior wall of described outer derivation channel setting body of heater, lower outside derivation feeder connection, upper outside derivation feeder connection leads to pyrolysis vaporizer through in the middle part of outer ring wall, outer derivation channel outlet leads to the raw gas concentration chamber at pyrolysis vaporizer top through outer ring wall, described derivation main channel is arranged in the exterior wall of the body of heater of coal heat decomposition stove, derive main channel inlets to communicate with raw gas concentration chamber and extend up to the exterior wall top arranging body of heater again and derive in circuit, derive circuit and be provided with raw gas export mouth, described as-fired coal spoil hot waste gas damping dewatering unit mainly comprises housing, steam steam discharge exporter, waste gas heat exchange dehydrator, blanking bin, form feed bin in described housing, feed bin relative closure top is only provided with opening for feed, and described blanking bin is arranged on housing bottom and communicates with feed bin, described steam steam discharge exporter comprises steam derives house steward, more than at least one steam derives umbrella road, vapor collection standpipe, water of condensation discharge manifold, it is umbrella shape inclination bending member that steam derives umbrella road, and many steam are derived umbrella road and are regularly horizontally installed in feed bin in interval, vapor collection standpipe is longitudinally arranged in the relative both sidewalls of housing, and steam is derived two ends, umbrella road and is separately fixed on both sidewalls vapor collection standpipe, bending member curved recessed in vapor collection standpipe on be provided with steam export mouth, steam is derived house steward and is arranged in the sidewall of the upper shell of vapor collection standpipe, steam is derived house steward and is communicated with vapor collection riser upper, steam is derived house steward and is also provided with water vapor relief outlet, water of condensation discharge manifold is arranged in the sidewall of below housing of vapor collection standpipe, water of condensation discharge manifold communicates with vapor collection standpipe bottom, and water of condensation discharge manifold is also provided with condensed water discharge outlet, described waste gas heat exchange dehydrator comprises hot waste gas admission passage, hot waste gas enters room, radiating pipe, radiating pipe serial connection passage, waste gas transition chamber, low temperature waste gas discharge chamber, the hot waste gas room of entering is arranged in middle and upper part one sidewall of housing, what waste gas transition chamber was arranged on housing enters in the relative another side sidewall in room with hot waste gas, low temperature waste gas discharge chamber is arranged on the bottom of housing and hot waste gas enters in the same face sidewall of room, and low temperature waste gas discharge chamber is provided with low temperature waste gas relief outlet, several radiating pipes serial connection passage parallel internal bin passing across housing between two, be connected on hot waste gas to enter between room and waste gas transition chamber and between waste gas transition chamber and low temperature waste gas discharge chamber, one end of upper radiating pipe serial connection passage communicates with the hot waste gas room of entering and the other end is closed, and one end of next radiating pipe serial connection passage is closed and the other end communicates with waste gas transition chamber, in like manner, between waste gas transition chamber and low temperature waste gas are discharged, also be that one end of upper radiating pipe serial connection passage communicates with waste gas transition chamber and the other end is closed, one end of next radiating pipe serial connection passage is closed and the other end communicates with low temperature waste gas discharge chamber, the rest may be inferred, several radiating pipes also adopt metallic substance to make, several radiating pipes are spaced on radiating pipe serial connection passage, the end that dispels the heat is connected on parallel upper radiating pipe serial connection passage, the other end be connected on parallel next radiating pipe serial connection passage on, by mutually through for radiating pipe parallel between two serial connection passage, room is entered and waste gas transition chamber is connected by hot waste gas, waste gas transition chamber and low temperature waste gas discharge chamber are connected, described tail gas water is washed one's hair cleaner and is comprised purification cylindrical shell, atomized spray, stainless steel filter wire stratum reticulare, tail gas pod, tank, water reservoir, sprinkling water pump, described purification cylindrical shell top arranges exhaust port, described atomized spray, stainless steel filtration silk screen, tail gas pod, tank all arrange in purification cylindrical shell, described water reservoir, spraying water pump, all to arrange purifying tube external, described tank arranges the bottom of purification cylindrical shell, and bottom of gullet is provided with spoil disposal pipeline, described tail gas pod is the top that the cylindrical cover of a lower ending opening upper end closed is arranged on tank, and tail gas water conservancy diversion is covered with a tail gas and enters pipe, and tail gas enters pipe and passes purification cylindrical shell and communicate with the external world, stainless steel filter wire stratum reticulare is provided with above tail gas pod, stainless steel filter wire stratum reticulare periphery is completely fixed on purifying tube body wall face, above stainless steel filter wire stratum reticulare, atomized spray is set, atomized spray is connected on water inlet pipe, water inlet pipe is connected with sprinkling water pump by water inlet supervisor, spray water pump and be connected to water absorption tube, water absorption tube stretches in water reservoir, water reservoir is also communicated with tank through purification cylindrical shell by communicating pipe, the raw gas of discharging from raw gas export mouth is purified, the outer gas-operated thermal bath facility of coal gangue pyrolysis installation delivered to again by raw gas after purification, interior gas-operated thermal bath facility burns, waste gas after burning delivers to the hot waste gas admission passage of the waste gas heat exchange dehydrator of as-fired coal spoil hot waste gas damping dewatering unit again by pipeline, the tail gas that the low temperature waste gas relief outlet of waste gas heat exchange dehydrator and tail gas water wash one's hair cleaner is entered pipe and connected by pipeline.
Described coal gangue pyrolysis installation also comprises gas reversing system, described outer gas-operated thermal bath facility is mainly some groups of structure identical association first combustion heaters, second combustion heater is formed, the first described combustion heater mainly comprises the first combustion chamber, first coal gas enters arm and the first regenerative heat exchanger, first coal gas enters arm and leads in the first combustion chamber through body of heater exterior wall, the body of heater exterior wall that first combustion chamber is made up of refractory materials and fire-resistant thermally conductive material make the gas-fired quirk that pyrolysis vaporizer's outer ring wall and outer quirk partition wall surround a relative closure, the first described regenerative heat exchanger comprises the first thermal, first heat storage, first air enters arm and the first combustion exhaust exhaust outlet, first thermal is arranged in body of heater exterior wall, first heat storage arranges in the first thermal, the first bottom of combustion chamber is led in first thermal one end, the other end is connected to the first air respectively and enters arm and the first combustion exhaust exhaust outlet, in like manner identical second combustion heater of structure also mainly comprises the second combustion chamber, second coal gas enters arm and the second regenerative heat exchanger, between the first described combustion chamber and second combustion chamber of next-door neighbour, outer quirk is provided with combustion chamber through hole every coping, first combustion chamber is connected to form with second combustion chamber of next-door neighbour and is associated one group by combustion chamber through hole, described interior gas-operated thermal bath facility is primarily of identical association the 3rd combustion heater of some groups of structures, 4th combustion heater, its structure with associate the first burning heater, second burning heater composition is almost identical, the 3rd combustion chamber unlike the 3rd combustion heater is made ringwall and internal-quirk partition wall in pyrolysis vaporizer by fire-resistant thermally conductive material and is surrounded the gas-fired quirk of a relative closure, 3rd coal gas enters passing beneath and upwards leading to the 3rd combustion chamber of article bow that arm bends from central supported, 3rd thermal is arranged on article body of heater of bow below, 3rd heat storage is placed in the 3rd thermal, the 3rd bottom of combustion chamber is led in the upwards extension that passes beneath of article bow that the 3rd thermal one end is bent from central supported by extension passage, the 3rd thermal the other end is connected to the 3rd air respectively and enters arm and the 3rd combustion exhaust exhaust outlet, between the 3rd described combustion chamber and the 4th combustion chamber of next-door neighbour, internal-quirk is provided with chamber passage every coping, 3rd combustion chamber is connected to form with the 4th combustion chamber of next-door neighbour and is associated one group by chamber passage, described gas reversing system comprises dish, lower wall, rotate reversing motor, air blower, gas fan, exhaust gas fan, lower wall is connected to an air supervisor respectively and the first air is in charge of, second air is in charge of, a coal gas supervisor and the first gas manifold, second gas manifold, a combustion exhaust supervisor and the second combustion exhaust are in charge of, first combustion exhaust is in charge of, wherein the second combustion exhaust is in charge of to be in charge of with the first combustion exhaust to be in charge of with the first air and is in charge of with the second air and the setting of the first gas manifold and the second gas manifold is just exchanged, upper dish is fitted in above lower wall, upper dish respectively correspondence is provided with air pipe connecting, gas connection pipes, combustion exhaust pipe connecting, rotate reversing motor and drive upper dish reciprocating rotation thus realize air supervisor and be constantly in charge of with the first air to be in charge of with the second air and carry out connecting and cutting off conversion on lower wall, coal gas supervisor constantly carries out connecting and cutting off conversion with the first gas manifold and the second gas manifold, combustion exhaust supervisor is constantly in charge of with the second combustion exhaust to be in charge of with the first combustion exhaust and carries out connecting and cutting off conversion, wherein, the first described air be in charge of enter arm with the first air, the 3rd air enter arm connect, simultaneously, the first described gas manifold and the first coal gas enter arm, the 3rd coal gas enters arm and connects, simultaneously now, the first described combustion exhaust is in charge of and is connected with the first combustion exhaust exhaust outlet, the 3rd combustion exhaust exhaust outlet, in like manner, second air be in charge of enter arm with the second air, the 4th air enter arm connect, simultaneously, second gas manifold and the second coal gas enter arm, the 4th coal gas enters arm and connects, meanwhile, the second burning gas is in charge of and is connected with the second combustion exhaust exhaust outlet, the 4th combustion exhaust exhaust outlet.
Described coal gangue pyrolysis installation also comprises the periphery that two groups of bustle pipes are arranged on body of heater, comprises the first air bustle pipe, the first coal gas bustle pipe, the first combustion exhaust bustle pipe; Second air bustle pipe, the second coal gas bustle pipe, the second combustion exhaust bustle pipe; The first wherein said air be in charge of enter arm by the first air bustle pipe and the first air, the 3rd air enter arm connect, simultaneously, the first described gas manifold enters arm by the first coal gas bustle pipe and the first coal gas, the 3rd coal gas enters arm and connects, simultaneously now, the first described combustion exhaust is in charge of and is connected with the first combustion exhaust exhaust outlet, the 3rd combustion exhaust exhaust outlet by the first combustion exhaust bustle pipe; In like manner, second air be in charge of enter arm by the second air bustle pipe and the second air, the 4th air enter arm connect, simultaneously, second gas manifold enters arm by the second coal gas bustle pipe and the second coal gas, the 4th coal gas enters arm and connects, meanwhile, the second burning gas is in charge of and is connected with the second combustion exhaust exhaust outlet, the 4th combustion exhaust exhaust outlet by the second combustion exhaust bustle pipe.
The exhaust gas fan of the gas reversing system of described coal gangue pyrolysis installation and the hot waste gas admission passage of as-fired coal spoil hot waste gas damping dewatering unit are connected by pipeline.
Described outer gas-operated thermal bath facility is mainly divided into the heating of upper, middle and lower segment formula, and every section has 9 groups of identical first combustion heaters of structure, the second combustion heater formation.
Described interior gas-operated thermal bath facility is mainly divided into the heating of upper and lower two-section type, and every section has 6 groups of identical 3rd combustion heaters of structure, the 4th combustion heater formation.
The radiating pipe of described waste gas heat exchange dehydrator is in " U " type, and the arrangement in two rows on radiating pipe serial connection passage of U-shaped radiating pipe, the U-shaped radiating pipe of a upper row is inverted U, and the U-shaped mouth of the U-shaped radiating pipe of a upper row is relative with the U-shaped mouth of the U-shaped radiating pipe of next row.
The external exhaust fan of low temperature waste gas relief outlet of described waste gas heat exchange dehydrator, exhaust fan washes one's hair cleaner again tail gas with tail gas water enters pipe and connects.
Purifying tube body wall face above described tank offers water-in, and the condensed water discharge outlet of the solidifying water discharge manifold of water-in and steam steam discharge exporter is connected by pipeline.
Described atomized spray, the stainless steel filter wire stratum reticulare order number that interval arranges one group of stainless steel filter wire stratum reticulare above in the of many groups from bottom to top in purification cylindrical shell is greater than the order number of the one group of stainless steel filter wire stratum reticulare in below.
The present invention is by carrying out high temperature pyrolysis to coal gangue and water-gas reaction obtains raw gas, raw gas is derived and purifies, heat and temperature that purified gas after purification provides to coal gangue pyrolytic gasification for burning, hot waste gas waste heat after utilizing burning again carries out damping dehydration to the coal gangue pellet entering stokehold, do not need to increase extra energy consumption, cost savings; Also can carry out cooling and dedusting to hot waste gas in addition, be beneficial to the " clean " exhaust gas that exhaust temperature in air is relatively low, preserve the ecological environment.
Accompanying drawing explanation
Below in conjunction with accompanying drawing, the specific embodiment of the present invention is described in further detail.
Fig. 1 is as-fired coal spoil hot waste gas damping dewatering unit cross-sectional schematic one of the present invention;
Fig. 2 is as-fired coal spoil hot waste gas damping dewatering unit cross-sectional schematic two of the present invention;
Fig. 3 is k-k place schematic cross-section in Fig. 1;
Fig. 4 is p-p place schematic cross-section in Fig. 1;
Fig. 5 is j-j place schematic cross-section in Fig. 1;
Fig. 6 is the cross-sectional schematic that tail gas water of the present invention washes one's hair cleaner;
Fig. 7 is the atomization gondola water faucet schematic cross-section (in Fig. 6 a-a) that tail gas water of the present invention washes one's hair cleaner;
Fig. 8 is the tail gas pod schematic cross-section (in Fig. 6 b-b) that tail gas water of the present invention washes one's hair cleaner;
Fig. 9 is the tank schematic cross-section (in Fig. 6 d-d) that tail gas water of the present invention washes one's hair cleaner;
Figure 10 is the bottom of gullet schematic cross-section (in Fig. 6 e-e) that tail gas water of the present invention washes one's hair cleaner;
Figure 11 is coal gangue pyrolytic gasification stove schematic diagram of the present invention;
Figure 12 is gas diverter schematic diagram of the present invention;
Gas diverter of the present invention coils schematic diagram to Figure 13;
Figure 14 is gas diverter lower wall schematic diagram of the present invention;
Figure 15 is c-c place cross-sectional schematic in Figure 13;
Figure 16 is gas diverter of the present invention and combustion heater pipe network connection diagram;
Figure 17 is t-t place schematic cross-section in Figure 11;
Figure 18 is u-u place schematic cross-section in Figure 11;
Figure 19 is v-v place schematic cross-section in Figure 11;
Figure 20 is central supported of the present invention bow schematic diagram (in Figure 11 x-x place schematic cross-section);
Figure 21 is vapour passage of the present invention intention (in Figure 11 y-y place schematic cross-section);
Figure 22 is steam pockets pipeline schematic diagram of the present invention (in Figure 11 z-z place schematic cross-section);
Figure 23 is industry control central electrical connection diagram of the present invention;
Figure 24 is that coal gangue pyrolytic gasification stove of the present invention and as-fired coal spoil hot waste gas damping dewatering unit and tail gas water wash one's hair cleaner assembly schematic diagram.
Embodiment
The specific embodiment of the comprehensive utilization of coal gangue pyrolytic gasification of the present invention is mainly introduced in detail following.
First part's coal gangue Task-size Controlling
Coal gangue processing is broken into 0 ~ 20mm granularity, dehydrates in this size range to coal gangue particle, fully dry, dewatering efficiency is high, but this is not formed the restriction of the present invention to required coal gangue.
The damping of second section coal gangue is dewatered
As shown in Figure 1 and Figure 2: as-fired coal spoil hot waste gas damping dewatering unit 1, comprises housing 11, steam steam discharge exporter 12, waste gas heat exchange dehydrator 13, blanking bin 14, the feed bin 111 being used for broken fed to boiler coal gangue pellet damping drying is formed in housing 11, feed bin 111 relative closure top is only provided with opening for feed 112, be provided with closed infeed belt conveyor 17 at opening for feed 112 place and (refer to the transfer roller covered by belt with its circumferential closed barrel-shaped casing of a both ends open, as-fired coal spoil is prevented to be scattered, keep Working environment neat and tidy), blanking bin 14 is arranged on bottom housing 11 and communicates with feed bin 111, blanking bin 14 is for temporarily depositing damping dried as-fired coal spoil pellet, closed discharge transfer roller 15 is connected to bottom blanking bin 14.
As shown in Figure 1, Figure 2, Fig. 3, shown in Fig. 4, Fig. 5, steam steam discharge exporter 12 comprises steam derives house steward 121, more than at least one steam and derives umbrella road 122, vapor collection standpipe 123, water of condensation discharge manifold 124; Steam derives umbrella road 122 in umbrella shape inclination bending member (maybe can be referred to as reverse V-shaped bending member), and many steam are derived umbrella road 122 and are regularly horizontally installed in feed bin 111 in interval; Vapor collection standpipe 123 is longitudinally arranged on housing 11 relatively in both sidewalls, and steam is derived two ends, umbrella road 122 and is separately fixed on both sidewalls vapor collection standpipe 123, bending member curved recessed in vapor collection standpipe 123 on be provided with steam export mouth 125; Steam is derived house steward 121 and is arranged in the sidewall of upper shell 11 of vapor collection standpipe 123, and steam is derived house steward 121 and communicated with vapor collection standpipe 123 top, and steam is derived house steward 121 and is also provided with water vapor relief outlet 126, is beneficial to the concentrated discharge of water vapor; Water of condensation discharge manifold 124 is arranged in the sidewall of below housing 11 of vapor collection standpipe 123, water of condensation discharge manifold 124 communicates with vapor collection standpipe 123 bottom, water of condensation discharge manifold 124 is also provided with condensed water discharge outlet 127, is beneficial to the concentrated discharge of water of condensation.
As Fig. 1, Fig. 2, shown in Fig. 3, high humidity when as-fired coal spoil pellet comes in just to come in from opening for feed 112, the steam produced is more, arrange more on feed bin 111 top so steam derives umbrella road 122, this example arranges the rule lateral arrangement of five row by three on feed bin 111 top, so that a large amount of steam is all derived smoothly, and in the middle part of feed bin 111 and bottom, as-fired coal spoil pellet water content after thermal dehydration is lower, the steam of evaporation is less, it is few with lower disposed in the middle part of feed bin 111 that steam derives umbrella road 122, this example is so arrange that in the middle part of feed bin 111 the steam derivation umbrella road 122 of five row arranged by material one, the steam arranging five row at feed bin 111 lower disposed material one derives umbrella road 122, certainly, the position that steam derivation umbrella road 122 is arranged in feed bin 111 and quantity depend primarily on the moisture degree of as-fired coal spoil pellet, the concrete structure that this example is enumerated does not form the claim limitation to this case.
As Fig. 1, Fig. 2, shown in Fig. 3, again because as-fired coal spoil pellet is come in falling into feed bin 111 from opening for feed 112, steam is derived umbrella road 122 and is regularly arranged in feed bin 111 in horizontal many of interval, steam derives umbrella road 122 in umbrella shape inclination bending member, as-fired coal spoil pellet is conducive to evenly to fall apart in feed bin 111, as-fired coal spoil pellet can thermally equivalent drying and dehydrating, again because steam export mouth 125 be arranged on steam derive umbrella road 122 bending member curved recessed in, can effectively prevent as-fired coal spoil pellet from blocking steam export mouth 125, the steam of deriving the curved recessed interior collection in umbrella road 122 through steam enters in vapor collection standpipe 123 by steam export mouth 125 smoothly, the steam of heat is upwards pooled in steam derivation house steward 121 by vapor collection standpipe 123 is discharged by water vapor relief outlet 126, steam is condensed into water because lowering the temperature, water is discharged from condensed water discharge outlet 127 by flowing into water of condensation discharge manifold 124 downwards.
As shown in Figure 1, Figure 2, shown in Fig. 4, Fig. 5, waste gas heat exchange dehydrator 13 comprises hot waste gas admission passage 131, hot waste gas enters room 132, radiating pipe 133, radiating pipe serial connection passage 134, waste gas transition chamber 135, low temperature waste gas discharge chamber 136, exhaust fan 137; Hot waste gas enters room 132 and is arranged in middle and upper part one sidewall of housing 11, and what waste gas transition chamber 135 was arranged on housing 11 enters in the relative another side sidewall in room 132 with hot waste gas; Low temperature waste gas discharge chamber 136 is arranged on the bottom of housing 11 and hot waste gas enters in the same face sidewall of room 132, and low temperature waste gas discharge chamber 136 is provided with low temperature waste gas relief outlet 138, the external exhaust fan 137 of low temperature waste gas relief outlet 138; Several radiating pipes serial connection passage 134 parallel internal bin 111 passing across housing 11 between two, be connected on hot waste gas to enter between room 132 and waste gas transition chamber 135 and between waste gas transition chamber 135 and low temperature waste gas discharge chamber 136, one end 1341 and the hot waste gas of upper radiating pipe serial connection passage 134 enter that room 132 communicates and the other end 1342 is closed, and one end 1341 of next radiating pipe serial connection passage 134 is closed and the other end 1342 communicates with waste gas transition chamber 135; In like manner, between waste gas transition chamber 135 and low temperature waste gas discharge chamber 136, also be that one end 1342 of upper radiating pipe serial connection passage 134 communicates with waste gas transition chamber 135 and the other end 1341 is closed, one end 1342 of next radiating pipe serial connection passage 134 is closed and the other end 1341 communicates with low temperature waste gas discharge chamber 136, the rest may be inferred, this example arranges many radiating pipes 133 and radiating pipe serial connection passage 134, to increase the contact area with stove coal gangue pellet, improves coal gangue dewatering particle collections efficiency.
As shown in Figure 1, Figure 2, shown in Fig. 4, Fig. 5, several radiating pipes 133 also adopt metallic substance to make, several radiating pipes 133 are spaced on radiating pipe serial connection passage 134, radiating pipe 133 is in " U " type, one end is connected on parallel upper radiating pipe serial connection passage 134, the other end be connected on parallel next radiating pipe serial connection passage 134 on, by mutually through for radiating pipe parallel between two serial connection passage 134, enter room 132 by hot waste gas to connect with waste gas transition chamber 135, waste gas transition chamber 135 and low temperature waste gas discharge chamber 136 are connected;
As shown in Figure 1 and Figure 2, the arrangement in two rows on radiating pipe serial connection passage 134 of U-shaped radiating pipe 133, the U-shaped radiating pipe 133 of a upper row is in inverted U, the U-shaped mouth of the U-shaped radiating pipe 133 of a upper row is relative with the U-shaped mouth of the U-shaped radiating pipe of next row 133, in order to be beneficial to coal gangue pellet blanking, the described upper U-shaped top of radiating pipe 133 in inverted U of row is wedge 1331, and the U-shaped inner bay place of the U-shaped radiating pipe of next row 133 is wedge 1332.
As shown in figure 11, infeed belt conveyor 17, discharge transfer roller 15, exhaust fan 137 are connected with industry control center 90, are automatically controlled the work of infeed belt conveyor 17, discharge transfer roller 15, exhaust fan 137 by industry control center 90.
This as-fired coal spoil hot waste gas damping dewatering is:
(1) closed infeed belt conveyor 17, is used to be sent to by the as-fired coal spoil pellet after fragmentation in the feed bin of housing 11 in 111 from coal inlet 112;
(2) hot waste gas, simultaneously produced after the purified gas burning after raw gas recovery of chemical products purification coal gangue high temperature pyrolysis and water-gas reaction produced passes into from hot waste gas admission passage 131 that heat is useless to enter room 132, flowed in radiating pipe 133 by radiating pipe serial connection passage 134 again and dewatered drying is carried out to the coal gangue of water content, hot waste gas reduces through heat-exchange temperature simultaneously, and last Low Temperature Thermal waste gas enters low temperature waste gas discharge chamber 136 by waste gas transition chamber 135 and discharges;
(3), coal gangue in the feed bin of housing 11 in 111 through radiating pipe 133 heated baking, water in coal gangue evaporates in a large number, water vapor is collected through steam derivation umbrella road 122 and is entered in vapor collection standpipe 123 by steam export mouth 125, the steam of heat is upwards pooled to steam is derived in house steward 121, concentrated by water vapor relief outlet 126 and discharge, the water vapor of the cooled cooling of a part becomes in the backward lower inflow water of condensation discharge manifold 124 of water of condensation and pools together, and discharges from condensed water discharge outlet 127;
(4) coal gangue after, dehydrating finally falls into the lower coal bunker 14 of housing 11 bottom, constantly the coal gangue dehydrated in lower coal bunker 14 is delivered to down one high temperature pyrolysis operation by closed discharge transfer roller 15, from and constantly to the feed bin 111 of housing 11, supplement new coal gangue pellet by closing infeed belt conveyor 17, realize the continuously dehydrating of coal gangue dry.
Wash one's hair cleaner 16 from the tail gas that low temperature waste gas discharge chamber 136 is discharged by tail gas water in order to keep the neat and tidy of environment and process rear qualified discharge.
As shown in Fig. 6, Fig. 7, Fig. 8, Fig. 9, Figure 10, tail gas water is washed one's hair cleaner 16 and is comprised purification cylindrical shell 161, atomized spray 162, stainless steel filter wire stratum reticulare 163, tail gas pod 164, tank 165, water reservoir 166, sprays water pump 167, purification cylindrical shell 161 top arranges exhaust port 168, and atomized spray 162, stainless steel filtration silk screen 163, tail gas pod 164, tank 165 all arrange in purification cylindrical shell 161, water reservoir 166, sprinkling water pump 167 all arrange outside purification cylindrical shell 161, tank 165 arranges the bottom of purification cylindrical shell 161, spoil disposal pipeline 1650 is provided with bottom tank 165, tail gas pod 164 is cylindrical cover of a lower ending opening upper end closed, tail gas pod 164 is arranged on the top of tank 165, tail gas pod 164 is provided with a tail gas and enters pipe 169, tail gas enter pipe 169 pass purification cylindrical shell 161 communicate with the external world, stainless steel filter wire stratum reticulare 163 is provided with above tail gas pod 164, stainless steel filter wire stratum reticulare 163 periphery is completely fixed on purification cylindrical shell 161 wall, above stainless steel filter wire stratum reticulare 163, atomized spray 162 is set, atomized spray 162 is connected on water inlet pipe 1601, water inlet pipe 1601 stretches out outside purification cylindrical shell 161 to be connected with water inlet bustle pipe 1602, water inlet bustle pipe 1602 is purify cylindrical shell 161 periphery in the form of a ring around the home, water inlet bustle pipe 1602 is connected with sprinkling water pump 167 by water inlet supervisor 160, spray water pump 167 and be connected to water absorption tube 1603, water absorption tube 1603 stretches in water reservoir 166, water reservoir 166 is also communicated with tank 165 through purification cylindrical shell 161 by communicating pipe 1604.
As shown in Figure 6, access opening 1611 is offered at purification cylindrical shell 161 wall above stainless steel filter wire stratum reticulare 163, one is facilitate workman to enter in purification cylindrical shell 161 atomized spray 162 damaged, stainless steel filter wire stratum reticulare 163 keeps in repair, two is also regularly can remove the plaster of alluvial on stainless steel filter wire stratum reticulare 163 by artificial, purification cylindrical shell 161 wall above tank 165 offers water-in 1612, this water-in 162 connects into the water of condensation discharge manifold 124 of the steam steam discharge exporter 12 of stove coal gangue hot waste gas damping dewatering unit 1 by pipeline, the water of condensation of the dust-laden allowing water of condensation discharge manifold 124 discharge directly enters uniform effluent in tank 165, ensure the clean of Working environment, offer into water overflow port 1613 at purification cylindrical shell 161 wall near tank 165 edge, the unnecessary water of tank 165 can be discharged from here, the water in tank 165 is avoided to flood the opening of tail gas pod 164 too much, cause tail gas to enter to be obstructed.
As Fig. 6, shown in Fig. 7, for to filtering dust in tail gas better, multiple atomized spray 162 161 to be arranged in the form of a ring in purification cylindrical shell, stretched out outside purification cylindrical shell 161 by many water inlet pipes 1601 and connect with water inlet bustle pipe 1602, in addition can also in purification cylindrical shell 161 from bottom to top interval many group atomized spray 162 are set, stainless steel filter wire stratum reticulare 163, and from bottom to top, the order number of stainless steel filter wire stratum reticulare 163 increases gradually, this tail gas water washes one's hair the atomized spray 162 that cleaner 16 is provided with 3 groups, stainless steel filter wire stratum reticulare 163, this not only can obtain cleaner tail gas, and can also lower the temperature to the tail gas of heat.
As shown in figure 11, spray water pump 167 to be connected, by the work of industry control center 90 automatic spraying water pump 167 with industry control center 90.
The Principle Method that this routine tail gas water washes one's hair purification is:
(1) low temperature waste gas of, discharging from the low temperature waste gas discharge chamber 136 of as-fired coal spoil hot waste gas damping dewatering unit 1 is through exhaust fan 137, tail gas is pumped into tail gas to enter pipe 169 and enter in tail gas pod 164, blow to the water surface in the tank 165 below tail gas pod 164, the dust that in tail gas, particle is larger, through the absorption of flow surface, is sunk to tank 165 end in the water of immersion tank and is discharged by spoil disposal pipeline 1650;
(2) tail gas, after flow surface absorption upwards filters through stainless steel filter wire stratum reticulare 163, elimination tail gas major part dust;
(3), after stainless steel filter wire stratum reticulare 163 filters tail gas enters the water smoke layer that atomized spray 162 water spray is formed again, through the exhaust port qualified discharge of water smoke layer cleaning by purification cylindrical shell 161 top in tail gas.
In order to allow discharge tail gas in dustiness be reduced to minimum, on it, (3) supplements further and is: after stainless steel filter wire stratum reticulare 163 filters, tail gas enters the water smoke layer that atomized spray 162 is formed again, the stainless steel filter wire stratum reticulare 163 upwards entering order number larger in tail gas after the cleaning of water smoke layer filters again, the water smoke layer cleaning that atomized spray 162 is formed above the stainless steel filter wire stratum reticulare 163 that this order number is larger again, finally by exhaust port 168 qualified discharge at purification cylindrical shell 161 top.
Part III coal gangue high temperature pyrolysis and gasification (pyrolysis heating, water-gas are sent out and answered)
The high temperature pyrolysis heating of first segment coal gangue
As shown in Figure 1, coal gangue pyrolysis installation 6 is arranged in the middle part of body of heater 91, mainly comprises pyrolysis vaporizer 61, outer gas-operated thermal bath facility 64, interior gas-operated thermal bath facility 67, gas reversing system 66, central supported bow 65 formation, as Fig. 8, shown in Fig. 9: pyrolysis vaporizer 61 is by fire-resistant thermally conductive material, outer ring wall 612, 611 form an annulus, being centered around pyrolysis vaporizer's exterior wall 611 ring periphery is outer gas-operated thermal bath facility 64, be interior gas-operated thermal bath facility 67 in ringwall 612 ring in pyrolysis vaporizer, wherein outer gas-operated thermal bath facility 64 is mainly first combustion heater 62 of some groups of (this example 9 groups) identical associations of structure, second combustion heater 60 forms (see Fig. 1, Fig. 2), as Fig. 1, Fig. 8, shown in Fig. 9: because pyrolysis vaporizer 61 is highly higher, wherein outer gas-operated thermal bath facility 64 is mainly divided into, in, lower Three-section type heating, every section of first combustion heater 62 having 9 groups of identical associations of structure, second combustion heater 60 is formed, interior gas-operated thermal bath facility 67 is mainly divided into, lower two-section type heating, every section has 6 groups of identical 3rd combustion heaters 68 mutually of structure, 4th combustion heater 69 is formed.
As Fig. 1, Fig. 9 show, the first described combustion heater 62 mainly comprises the first combustion chamber 621, first coal gas and enters arm 622 and the first regenerative heat exchanger 624, first coal gas and enter arm 622 and lead in the first combustion chamber 621 through body of heater 91 exterior wall.
As shown in Fig. 1, Fig. 9: body of heater 91 exterior wall that the first combustion chamber 621 is made up of refractory materials and fire-resistant thermally conductive material make the gas-fired quirk that pyrolysis vaporizer's outer ring wall 611 and outer quirk partition wall 625 surround a relative closure.
As shown in Fig. 1, Fig. 9, the first regenerative heat exchanger 624 comprises the first thermal 626, first heat storage 623, first air and enters arm 627 and the first combustion exhaust exhaust outlet 628; First thermal 626 is arranged in body of heater 91 exterior wall, first heat storage 623 arranges in the first thermal 626, first thermal 626 one end is led to bottom the first combustion chamber 621, and the other end is connected to the first air respectively and enters arm 627 and the first combustion exhaust exhaust outlet 628.
As shown in Figure 9, enter at the first air and to be provided with the first one-way air valve 629, first one-way air valve 629 between arm 627 and the first thermal 626 and to allow air to enter pipe 627 from the first air and the first thermal 626 flows into the first combustion chamber 621; The first unidirectional waste gas valve 620 is provided with between the first combustion exhaust exhaust outlet 628 and the first thermal 626, first unidirectional waste gas valve 620 allows gas-fired waste gas to flow through the first thermal 626 from the first combustion chamber 621, finally discharge (certainly from the first combustion exhaust exhaust outlet 628, adopt gas reversing system 66 as described below, when air supervisor 667 and the first air are in charge of 6671 connections, air supervisor 667 and the second air are in charge of 6673 and are in cut-out; Meanwhile, combustion exhaust supervisor 669 is in charge of 6691 with the first combustion exhaust and also cuts off mutually, and corresponding combustion exhaust supervisor 669 and the second combustion exhaust are in charge of 6693 and are in and are connected, the effect of replacement first one-way air valve 629 and the first unidirectional waste gas valve 620 can be played).
In like manner, as shown in Figure 9: identical second combustion heater 60 of structure mainly comprises the second combustion chamber 601, second coal gas and enters arm 602 and the second regenerative heat exchanger 604.
As shown in Figure 9: body of heater 91 exterior wall that the second combustion chamber 601 is made up of refractory materials and fire-resistant thermally conductive material make the gas-fired quirk that pyrolysis vaporizer's outer ring wall 611 and outer quirk partition wall 625 surround a relative closure.
As shown in Fig. 1, Fig. 9: the second coal gas enters arm 602 and leads in the first combustion chamber 601 through body of heater 91 exterior wall.
As shown in Figure 9: the second regenerative heat exchanger 604 comprises the second thermal 606, second heat storage 603, second air enters arm 607 and the second combustion exhaust exhaust outlet 608, second thermal 606 is arranged in body of heater 91 exterior wall, second heat storage 603 arranges in the second thermal 606, second thermal 606 one end is led to bottom the second combustion chamber 601, the other end is connected to the second air respectively and enters arm 607 and the second combustion exhaust exhaust outlet 608, enter between arm 607 and the second thermal 606 at the second air and be provided with the second one-way air valve 609, second one-way air valve 609 allows air to enter pipe 607 from the second air and the second thermal 606 flows into the second combustion chamber 601, the second unidirectional waste gas valve 600 is provided with between the second combustion exhaust exhaust outlet 608 and the second thermal 606, second unidirectional waste gas valve 600 allows gas-fired waste gas to flow through the second thermal 606 from the second combustion chamber 601, finally discharge (certainly from the second combustion exhaust exhaust outlet 608, adopt gas reversing system 66 as described below, when air supervisor 667 and the first air are in charge of 6671 cut-outs, air supervisor 667 and the second air are in charge of 6673 and are in connection, meanwhile, combustion exhaust supervisor 669 and the first combustion exhaust are in charge of 6691 and are also connected, and corresponding combustion exhaust supervisor 669 is in charge of 6693 with the second combustion exhaust and also cuts off mutually, the effect of replacement second one-way air valve 609 and the second unidirectional waste gas valve 600 can be played).
As shown in Fig. 1, Fig. 8, between second combustion chamber 601 of the first combustion chamber 621 and next-door neighbour, the top of outer quirk partition wall 625 is provided with combustion chamber through hole 6251, first combustion chamber 621 and second combustion chamber 601 of next-door neighbour are connected to form and are associated one group by combustion chamber through hole 6251, in this example, outer gas-operated thermal bath facility 64 is provided with quirk partition wall 625 partition wall outside 18 roads altogether, forms 9 groups of association burning groups; In addition, as shown in Figure 1; Because pyrolysis vaporizer 61 is highly higher, wherein outer gas-operated thermal bath facility 64 is mainly divided into the heating of upper, middle and lower segment formula, and every section has 9 groups of structures identical and associates the first combustion heater 62, second combustion heater 60 and forms.
As shown in Figure 1: on body of heater 91 exterior wall, each combustion chamber is also provided with chamber temperature monitoring holes 6201 and combustion chamber spy hole 6202, combustion chamber spy hole 6202 is convenient to the gas-fired situation of each combustion chamber of technician's direct vision, chamber temperature table 6203 is provided with for the temperature monitoring to combustion chamber, so that the assessment to pyrolysis of coal process in chamber temperature monitoring holes 6201.
As shown in Figure 3: chamber temperature table 6203 and industry control center 90 are connected, the temperature data of chamber temperature table 6203 is automatically gathered by industry control center 90.
As Fig. 2, Fig. 3, Fig. 4, Fig. 5, Fig. 6, gas reversing system 66 comprises dish 661, lower wall 662, rotate reversing motor 663, air blower 664, gas fan 665, exhaust gas fan 666, lower wall 662 is connected to an air supervisor 667 respectively and the first air is in charge of 6671, second air is in charge of 6673, a coal gas supervisor 668 and the first gas manifold 6681, second gas manifold 6683, a combustion exhaust supervisor 669 and the second combustion exhaust are in charge of 6693, first combustion exhaust is in charge of 6691, wherein, second combustion exhaust be in charge of 6693 and first combustion exhaust be in charge of 6691 and first air be in charge of 6671 and second air be in charge of 6673 and first the setting of gas manifold 6681 and the second gas manifold 6683 just exchange (Fig. 3, Fig. 4, shown in Fig. 6).
As Fig. 3, Fig. 4, Fig. 5, shown in Fig. 6: upper dish 661 is fitted in above lower wall 662, upper dish 661 respectively correspondence is provided with air pipe connecting 6672, gas connection pipes 6682, combustion exhaust pipe connecting 6692, rotate reversing motor 663 drive upper dish 661 on lower wall 662 reciprocating rotation thus realize air supervisor 667 be constantly in charge of with the first air 6671 and second air be in charge of 6673 and carry out connecting and cutting off conversion, coal gas supervisor 668 constantly carries out connecting and cutting off conversion with the first gas manifold 6681 and the second gas manifold 6683, combustion exhaust supervisor 669 be constantly in charge of with the second combustion exhaust 6693 and first combustion exhaust be in charge of and 6691 carry out connecting and cut off and change (with the first air be in charge of 6671 and second air be in charge of 6673 and first the switching of gas manifold 6681 and the second gas manifold 6683 just contrary).
As shown in Fig. 1, Fig. 6, be also provided with two groups of bustle pipes in the periphery of body of heater 91, comprise the first air bustle pipe 6674, first coal gas bustle pipe 6684, first combustion exhaust bustle pipe 6694; Second air bustle pipe 6675, second coal gas bustle pipe 6685, second combustion exhaust bustle pipe 6695.
As shown in Fig. 1, Fig. 6, first air bustle pipe 6,674 first air is in charge of 6671 and first air enter arm 627 and link up, the first air is in charge of the 6671, first air bustle pipe 6674, first air and enters arm 627, first thermal 626 and the first combustion chamber 621 forms same path;
Meanwhile, the first gas manifold 6681 and the first coal gas are entered arm 622 and link up by the first coal gas bustle pipe 6684, the first gas manifold 6681, first coal gas bustle pipe 6684, first coal gas are entered arm 622 and the first combustion chamber 621 forms same path;
Simultaneously now, first combustion exhaust bustle pipe 6694 be the first combustion exhaust is in charge of 6691 and first combustion exhaust exhaust outlet 628 link up, the first combustion exhaust is in charge of the 6691, first combustion exhaust bustle pipe 6694, first combustion exhaust exhaust outlet 628, first thermal 626 and forms same path with combustion chamber 621.
In like manner, second air bustle pipe 6,675 second air is in charge of 6673 and second air enter arm 607 and link up, the second air is in charge of the 6673, second air bustle pipe 6675, second air and enters arm 607, second thermal 606 and the second combustion chamber 601 forms same path;
Meanwhile, the second gas manifold 6683 and the second coal gas are entered arm 602 and link up by the second coal gas bustle pipe 6685, the second gas manifold 6683, second coal gas bustle pipe 6685, second coal gas are entered arm 602 and the second combustion chamber 601 forms same path;
Meanwhile, second combustion exhaust bustle pipe 6,695 second burning gas is in charge of 6693 and second combustion exhaust exhaust outlet 608 link up, the second combustion exhaust is in charge of the 6693, second combustion exhaust bustle pipe 6695, second combustion exhaust exhaust outlet 608, second thermal 606 and the second combustion chamber 601 forms same path.
In addition; as shown in Figure 3; this example also comprises gas reversing system controller 906 for controlling rotation reversing motor 663, air blower 664, gas fan 665, exhaust gas fan 666; gas reversing system electric controller 906 is connected with upper industry control center 90 again; certainly from electric control theory; rotate reversing motor 663, air blower 664, gas fan 665, exhaust gas fan 666 in this example also can directly control by industry control center 90, so arrange gas reversing system controller 906 herein do not form restriction to this routine protection domain.
Shown in as shown in Figure 1, Figure 2 ~ Fig. 5, Fig. 6, Fig. 3: the heating means of this outer gas-operated thermal bath facility 64 are:
(1) industry control center 90 starts and rotates reversing motor 663 and drive upper dish 661 to rotate on lower wall 662, and air supervisor 667 and the first air are in charge of 6671 connections, air be responsible for 667 and second air be in charge of 6673 and be in dissengaged positions; Meanwhile, coal gas supervisor 668 and the first gas manifold 6681 are also connected, and coal gas supervisor 668 and the second gas manifold 6683 are in dissengaged positions; Meanwhile, combustion exhaust supervisor 669 is in charge of 6691 with the first combustion exhaust and also cuts off mutually, and corresponding combustion exhaust be responsible for 669 and second combustion exhaust be in charge of 6693 and be in the state of being connected;
(2) industry control center 90 starts air blower 664, gas fan 665, exhaust gas fan 666, air is blasted air supervisor 667 by air blower 664, air passes into air pipe connecting 6672, first air successively and is in charge of the 6671, first air bustle pipe 6674, first air and enters arm 627 and enter into the first thermal 626, enters in the first combustion chamber 621 after the heat utilizing the first heat storage 623 to discharge heats air, simultaneously, raw gas is obtained purified gas and blasts coal gas supervisor 668 by gas fan 665 after recovery of chemical products purification, coal gas enters gas connection pipes 6682 successively, first gas manifold 6681, first coal gas bustle pipe 6684, first coal gas enters arm 622 and enters in the first combustion chamber 621 and burn, meanwhile, because combustion exhaust supervisor 669 is in charge of 6691 with the first combustion exhaust and is in phase dissengaged positions, and corresponding combustion exhaust supervisor 669 and the second combustion exhaust are in charge of 6693 and are in the state of being connected, so the waste gas in the first combustion chamber 621 after gas-fired can only enter into the second combustion chamber 601 by the combustion chamber through hole 6251 on outer quirk partition wall 625 top, again in the second thermal 606, carry out after absorbing and cooling temperature from the second combustion exhaust exhaust outlet 608 through the second heat storage 603 in the second thermal 606, second combustion exhaust bustle pipe 6695, second combustion exhaust is in charge of 6693, combustion exhaust supervisor 669 is discharged by exhaust gas fan 666,
(3) reach setting combustion time, industry control center 90 starts rotation reversing motor 663 and drives upper dish 661 to rotate backward on lower wall 662, air supervisor 667 and the first air are in charge of 6671 cut-outs, air supervisor 667 and the second air are in charge of 6673 and are in on-state, simultaneously, coal gas supervisor 668 also cuts off mutually with the first gas manifold 6681, coal gas supervisor 668 and the second gas manifold 6683 on-state, meanwhile, combustion exhaust supervisor 669 and the first combustion exhaust are in charge of 6691 and are also connected, and corresponding combustion exhaust supervisor 669 and the second combustion exhaust are in charge of 6693 also phase dissengaged positions,
(4) air is blasted air supervisor 667 by air blower 664, air passes into air pipe connecting 6672, second air successively and be in charge of the 6673, second air bustle pipe 6675, second air and enter arm 607 and enter into the second thermal 606, enters in the second combustion chamber 601 after the heat utilizing the second heat storage 603 in the second thermal 606 to discharge heats air, simultaneously, gas fan 665 by raw gas through recovery clean after obtain purified gas and blast coal gas supervisor 668, coal gas enters gas connection pipes 6682 successively, second gas manifold 6683, second coal gas bustle pipe 6685, second coal gas enters arm 602 and enters in the second combustion chamber 601 and burn, meanwhile, because combustion exhaust supervisor 669 and the first combustion exhaust are in charge of 6691 and are connected, and corresponding combustion exhaust supervisor 669 and the second combustion exhaust are in charge of 6693 and are in phase dissengaged positions, so the waste gas in the second combustion chamber 601 after gas-fired can only enter in the first combustion chamber 621 by the combustion chamber through hole 6251 on outer quirk partition wall 625 top, again through the first thermal 626, after the first heat storage 603 in the first thermal 626 carries out absorbing and cooling temperature, last from the first combustion exhaust exhaust outlet 628, first combustion exhaust bustle pipe 6694, first combustion exhaust is in charge of 6691, combustion exhaust supervisor 669 is discharged by exhaust gas fan 666, so outer gas-operated thermal bath facility 64 combustion principle is when the waste gas generated after gas-fired in the first combustion chamber 621 enters the second combustion chamber 601 from combustion chamber through hole 6251, discharge after the cooling of its exhaust-heat absorption through the second heat storage 603 in the second combustion chamber 601 and the second thermal 606, otherwise, when the waste gas generated after gas-fired in the second combustion chamber 601 enters the first combustion chamber 621 from combustion chamber through hole 6251, discharge after the cooling of its exhaust-heat absorption through the first heat storage 603 in the first combustion chamber 621 and the first thermal 606.
In sum, this gas two by gas reversing system enters the mode of operation of the regenerative heat exchange of a mode of operation out and regenerative heat exchanger, realize the combustion heater alternate combustion of two groups of associations, namely gas reversing system sends into air, purified gas burning to the combustion chamber of the first combustion heater, hot waste gas simultaneously from the combustion chamber of the second combustion heater after sucking-off burning, the second heat storage absorbing and cooling temperature of hot waste gas in the second regenerative heat exchanger of the second combustion heater becomes the relatively low low temperature waste gas of temperature and discharges; In like manner, gas reversing system sends into air, purified gas burning to the combustion chamber of the second combustion heater, hot waste gas simultaneously from the combustion chamber of the first combustion heater after sucking-off burning, the first heat storage absorbing and cooling temperature of hot waste gas in the first regenerative heat exchanger of the first combustion heater becomes the relatively low low temperature waste gas of temperature and discharges; This mutually utilize gas-fired after waste gas residual heat carry out adding the method for warm air, both served the waste gas residual heat after to gas-fired to make full use of, improve the efficiency of combustion of the coal gas in combustion chamber, the cooling carrying out to a certain degree to the waste gas after gas-fired again, the external energy need not be consumed, play energy-saving and cost-reducing object, save coal gangue pyrolytic gasification cost.
Automatically controlled by the heating of external gas-operated thermal bath facility 64, reduce human cost, improve the control accuracy to pyrolysis of coal process, realize automatization.
As Fig. 1, shown in Figure 10, interior gas-operated thermal bath facility 67 is primarily of some groups of (this example 6 groups) combustion heaters 68 that structure is identical, 69, because the highly higher interior gas-operated thermal bath facility 67 of pyrolysis vaporizer 61 is primarily of being mainly divided into, lower two-section type heating, every section has association the 3rd combustion heater 68 that 6 groups of structures are identical, 4th combustion heater 69, its composition structure and combustion principle associate the first burning heater 62 with above introduction, second burning heater 60 is almost identical, 3rd combustion heater 68 also comprises the 3rd combustion chamber 681, 3rd coal gas enters arm 682, 3rd thermal 686, 3rd heat storage 683, 3rd air enters arm 687 and the 3rd combustion exhaust exhaust outlet 688.
As shown in Fig. 1, Fig. 9, Figure 10, the 3rd combustion chamber 681 is made ringwall 612 and internal-quirk partition wall 635 in pyrolysis vaporizer by fire-resistant thermally conductive material and is surrounded the gas-fired quirk of a relative closure.
As shown in Figure 1, Figure 10 shows, 3rd coal gas of hypomere enters arm 682 and upwards leads to the 3rd combustion chamber 681 from article passing beneath of bow 651 for central supported bow 65,3rd thermal 686 is arranged on the body of heater 91 below article bow 651,3rd heat storage 683 is placed in the 3rd thermal 686,3rd thermal 686 one end is led to bottom the 3rd combustion chamber 681 by extending passage 6861 from the upwards extension that passes beneath of article bow 651 of central supported bow 65, and the 3rd thermal 686 the other end is connected to the 3rd air respectively and enters arm 687 and the 3rd combustion exhaust exhaust outlet 688.
As Fig. 1, Fig. 9, shown in Figure 10, 3rd coal gas of epimere enters arm 682 and upwards leads to the 3rd combustion chamber 681 through quirk partition wall 635 from article passing beneath of bow 651 for central supported bow 65, 3rd thermal 686 is arranged on the body of heater 91 below article bow 651, 3rd heat storage 683 is placed in the 3rd thermal 686, 3rd thermal 686 one end is upwards led to bottom the 3rd combustion chamber 681 through quirk partition wall 635 extension by extending passage 6861 from the passing beneath of article bow 651 of central supported bow 65, 3rd thermal 686 the other end is connected to the 3rd air respectively and enters arm 687 and the 3rd combustion exhaust exhaust outlet 688.
In like manner, as shown in Figure 9, Figure 10,4th combustion heater 69 structure is complete identical with the 3rd combustion heater 68, repeats no more here, and wherein the 4th combustion chamber 691 and the 3rd combustion chamber 681 are connected to form by chamber passage 6305 and associated one group (shown in Fig. 1, Fig. 8).
Wherein, as shown in Figure 6,3rd coal gas of the 3rd combustion chamber 681 of the 3rd burning heater 68 enters arm 682, the 3rd air enters arm 687 and the 3rd combustion exhaust exhaust outlet 688 is in charge of the 6671, first combustion exhaust respectively by the first coal gas bustle pipe 6684, first air bustle pipe 6674, first combustion exhaust bustle pipe 6694 and the first gas manifold 6681, first air and is in charge of 6691 and communicates.
As shown in Fig. 1, Fig. 6, Figure 10, the 4th coal gas of the 4th combustion chamber 691 of the 4th burning heater 69 enters arm 692, the 4th air enters arm 697 and the 4th combustion exhaust exhaust outlet 698 is in charge of the 6673, second combustion exhaust respectively by the second coal gas bustle pipe 6685, second air bustle pipe 6675, second combustion exhaust bustle pipe 6695 and the second gas manifold 6683, second air and is in charge of 6693 and communicates.
In sum, the 3rd burning heater 68, the 4th combustion heater 69 combustion principle are almost identical with above first burning heater 62, second burning heater 60, repeat no more here.
As shown in Figure 1, Figure 10 shows, central supported bow 65, because the quirk partition wall 635 of ringwall 612 and combustion heating unit 67 is all arranged in furnace chamber in pyrolysis vaporizer, needs central supported to bend 65 and provide support for it, provide the laying of various pipeline to again combustion heating unit 67 simultaneously.
As shown in Figure 1, Figure 10 shows, central supported bow 65 is arranged in the furnace chamber below pyrolysis vaporizer 61, combustion heating unit 67, mainly comprise bar bow 651, the Huo Gong center ringwall 652 of some, bar bends 651 one end and is fixed on Huo Gong center ringwall 652, the other end is fixed on body of heater 91, bar bow 651 around ringwall 652 center, Huo Gong center at a certain angle spaced radiation shape to scatter layout, fire bow 651 in this example is 12 bows, and quantity is consistent with the 3rd burning heater 68 the 4th burning heater 69 sum that is mutually related of combustion heating unit 67.
As shown in Figure 1, Figure 10 shows, article one, fiery bow in the body of wall of 651 arranges the extension passage 6861 that the 3rd coal gas enters arm 682 and the 3rd thermal 686, tightly adjacent another bar fire bends the extension passage 6961 that the 4th coal gas arranged in the body of wall of 651 enters arm 692 and the 4th thermal 696, provide convenience to the pipeline laying of combustion heating unit 67, make the various conduit arrangements of combustion heating unit 67 orderly, be unlikely to interfere.
Second section water-gas reaction
Because coal gangue temperature in pyrolysis vaporizer is higher, then pass into water vapor to coal gangue, the charcoal in coal gangue pyrolysis after product and superheated vapour meet and carry out water-gas reaction and generate water-gas (carbon monoxide and hydrogen).
As shown in Fig. 1, Figure 10, Fig. 1, water-gas reaction device 7 comprises pyrolysis vaporizer 61, material heat sink 70, steam generation device 75.
As shown in Figure 1, pyrolysis vaporizer 61 is positioned at above central supported bow 65, and material heat sink 70, steam generation device 75 are positioned at below central supported bow 65.
As shown in Fig. 1, Fig. 1, material heat sink 70 is arranged on and stretches out body of heater 91 bottom, comprises high temperature reduction chamber 701, low temperature cooling chamber 702, reduction chamber bridge arch 703; The top of high temperature reduction chamber 701 communicates with bottom pyrolysis vaporizer 61; High temperature reduction chamber 701 is setting up and down with low temperature cooling chamber 702, and reduction chamber bridge arch 703 is arranged between high temperature reduction chamber 701 and low temperature cooling chamber 702, and reduction chamber bridge arch 703 comprises bridge bow 7031, steam chest 704, steam enter siphunculus 707; Article 4, bridge bow 7031 is partitioned into spoke shape layout at an angle with high temperature reduction chamber 701 and low temperature cooling chamber 702 axle center, steam chest 704 is formed in the middle part of bridge bow 7031, steam chest 704 is a cylindrical chamber, the top of steam chest 704 is provided with semisphere blast cap 708, and the lower openings of steam chest 704 is towards low temperature cooling chamber 702; Steam enters siphunculus 707 and is arranged in bridge bow 7031, and steam enters siphunculus 707 one end and leads to steam chest 704, and the other end stretches out outside body of heater 91.
As Fig. 1, shown in Fig. 2, steam generation device 75 comprises annular hollow metal box body 755, steam pockets 754 and drum input tube 751, drum output tube 752, annular hollow metal box body 755 is arranged on bottom body of heater 91, the inner ring cavity 758 of annular hollow metal box body 755 is connected to low temperature cooling chamber 702 bottom of material heat sink 70, the big up and small down funnel-form of inner ring cavity 758 annular cavity, the body of heater water bag 753 that opposing seal is used for storage of water is formed in annular hollow metal box body 755 casees, body of heater water bag 753 is connected to water inlet pipe 756 and drum input tube 751, water inlet pipe 756 communicates with water tank 757, drum input tube 751 and steam pockets 754 are connected, drum output tube 752 and the steam of material heat sink 70 of steam pockets 754 enter siphunculus 707 the other end and communicate.
Water-gas reaction Principle Method of the present invention is:
(1), in steam pockets 754, water vapor enters siphunculus 707 by drum input tube 752 and steam and passes into water vapor to the low temperature cooling chamber 702 of material heat sink 70, water vapor blows to low temperature cooling chamber 702, except lowering the temperature to the solid product after pyrolytic gasification in low temperature cooling chamber 702, water vapor upwards seals in high temperature reduction chamber 701, give and fall into the cooling of the high-temp solid product after a large amount of pyrolytic gasification of high temperature reduction chamber 701 from pyrolysis vaporizer 61, while the solid of water vapor after giving pyrolytic gasification carries out lowering the temperature, improve vapor temperature and form superheated vapour;
(2), superheated vapour enters pyrolysis vaporizer 61 through central supported bow 65, and contact with the high-temperature coal spoil pyrolysis material of pyrolysis vaporizer 61, the charcoal after coal gangue pyrolysis in solid product and superheated vapour meet and carry out water-gas reaction and generate water-gas (carbon monoxide and hydrogen);
(3), solid product after coal gangue pyrolytic gasification falls into high temperature reduction chamber 701 and the low temperature cooling chamber 702 of material heat sink 70 from pyrolysis vaporizer 61, overheated high-temperature water vapor is heated as again to the water vapor upwards entering pyrolysis vaporizer 61 through low temperature cooling chamber 702 and high temperature reduction chamber 701, again the solid product after coal gangue pyrolytic gasification is lowered the temperature simultaneously, in recycling low temperature cooling chamber 702, solid product waste heat adds thermosetting water vapor to the water in body of heater water bag 753, water vapor enters in steam pockets 754 by drum input tube 751, to supplementing a large amount of water vapors consumed because of water-gas reaction in steam pockets 754, water-gas reaction can uninterruptedly be carried out continuously.
It is carry out in pyrolysis vaporizer 61 middle and lower part that water-gas reaction of the present invention generates in a large number, this is because the coal gangue pyrolysis in this section of pyrolysis vaporizer is relatively abundant, temperature is also relatively high, now pass into the water vapor of hyperthermia and superheating from the bottom of pyrolysis vaporizer 61, the charcoal in the solid product after overheated water vapor and coal gangue pyrolysis swashs mutually will produce a large amount of water-gas; Certainly, water vapor is being given in the solid product temperature-fall period in high temperature reduction chamber 701 and low temperature cooling chamber 702 after coal gangue pyrolytic gasification, also water-gas can be produced with charcoal remaining in the solid product after coal gangue pyrolytic gasification, but the amount produced is relatively little, this height of charcoal remaining in solid product after this and coal gangue pyrolytic gasification is few, and steam temperature neither be too high relevant.
The present invention utilizes the waste heat of the relatively low solid product of the temperature after coal gangue pyrolytic gasification to carry out heat trnasfer and produces water vapor, the solid product that recycling water vapor is higher with temperature directly contacts generation superheated vapour, reach the temperature required of water-gas reaction, promote that water-gas reaction fills part more, both while reduction solid product temperature, produce water vapor and superheated vapour again, thisly do not need to consume that the technological method of additional energy source meets that we advocate today is energy-saving and cost-reducing, the theory of Sustainable development.
Section three, raw gas take-up gear
Coal gangue produces the gas containing a lot of useful composition in high temperature pyrolysis and gasification process, charcoal in coal gangue pyrolysis after product and superheated vapour carry out water-gas reaction and generate water-gas (carbon monoxide and hydrogen), more than be referred to as raw gas, need to derive to utilize raw gas.
As shown in Fig. 1, Fig. 8, Fig. 9, raw gas take-up gear 8, comprises raw gas concentration chamber 81, interior derivation passage 82, and outer derivation passage 83, derivation main channel 84, derive circuit 85; Raw gas concentration chamber 81 be arranged on the top of pyrolysis vaporizer 61 and pyrolysis vaporizer 61 integrally formed; As shown in Fig. 1, Fig. 8, article 6, deriving passage 82 in arranges in quirk partition wall 635, interior derivation feeder connection 821 leads to pyrolysis vaporizer 61 through in the middle part of interior ringwall 612, and interior derivation channel outlet 822 leads to the raw gas concentration chamber 81 at pyrolysis vaporizer top through interior ringwall 612; As shown in Fig. 1, Fig. 8, article 6, outer passage 83 of deriving arranges in the exterior wall of body of heater 91, lower outside derivation feeder connection 831, upper outside derivation feeder connection 834 lead to pyrolysis vaporizer 61 through in the middle part of outer ring wall 611, and outer derivation channel outlet 832 leads to the raw gas concentration chamber 81 at pyrolysis vaporizer top through outer ring wall 611.
As shown in Figure 1, Figure 7 shows, deriving main channel 84 is arranged in the exterior wall of body of heater 91 of coal heat decomposition stove, derive main channel inlets 841 to communicate with raw gas concentration chamber 81 and extend up to the exterior wall top arranging body of heater 91 again and derive in circuit 85, derivation circuit 85 is provided with raw gas export mouth 851, raw gas export mouth 852.
As Fig. 1, Fig. 7, Fig. 8, shown in Fig. 9, because pyrolysis vaporizer 61 annular chamber in this example, so raw gas concentration chamber 81 also corresponding annular chamber, article 6, deriving passage 82 in is separately positioned in 6 road quirk partition walls 635, pyrolysis vaporizer 61 is led to through interior ringwall 612, article 6, outer derivation passage 83 is separately positioned in the middle of body of heater 91 exterior wall and leads to pyrolysis vaporizer 61 through with outer quirk partition wall 625 and outer ring wall 611, wherein, because the circumference of pyrolysis vaporizer 61 is longer, so in pyrolysis vaporizer 61 ringwall 612, outer ring wall 611 is respectively arranged with in 6 and derives feeder connection 821 and lower outside derivation feeder connection 831, upper outside derivation feeder connection 834, again because the height of pyrolysis vaporizer 61 is high, interior derivation feeder connection 821 and lower outside derivation feeder connection 831, upper outside derivation feeder connection about 834 staggers setting, as shown in Figure 1, interior derivation feeder connection 821 is higher than lower outside derivation feeder connection 831, but lower than upper outside derivation feeder connection 834 place, this example adopts this structure can better can derive the raw gas that section different in pyrolysis vaporizer 61 produces, also be provided with 6 larger raw gas main channels 84 of sectional area around raw gas concentration chamber 81 in addition and lead to derivation circuit 85, the object of such setting conveniently can derive a large amount of raw gas in raw gas concentration chamber 81.
As shown in Figure 1, the exterior wall of body of heater 91 is provided with the raw gas temperature monitoring holes 811 leading to raw gas concentration chamber 81, in raw gas temperature monitoring holes 811, places raw gas temperature table 812.
As shown in Figure 3, raw gas temperature table 812 and industry control center 90 are electrically connected, and temperature in raw gas concentration chamber 81 is monitored by raw gas temperature table 812 in industry control center 90.
The raw gas that section different in pyrolysis vaporizer 61 produces enters interior derivation passage 82 from interior derivation feeder connection 821 by this routine feature respectively, enter outer derivation passage with lower outside derivation feeder connection 831, upper outside derivation feeder connection 834 to go out in 83 to collect in raw gas concentration chamber 81 again, a large amount of raw gas in certain pyrolysis vaporizer 61 directly rise up in raw gas concentration chamber 81, entering derivation circuit 85 by deriving main channel 84, finally discharging from raw gas export mouth 851.
Section four, continuous pyrolysis gasification
Comprehensively above-mentioned, this routine feature is that coal gangue pyrolysis, gasification (water-gas reaction), steam generation, raw gas are derived process integration in same body of heater, makes coal gangue pyrolysis, gasification (water-gas reaction), steam generation, raw gas be able to continuous realization.
As shown in Figure 1, coal gangue pyrolytic gasification stove 9 comprise body of heater 91, enter furnace charge storehouse 92, coal gangue pyrolysis gasifying device 93, raw gas take-up gear 8, hinge cage sealing discharging device 96, product feed bin 94, coal gangue pyrolysis gasifying device 93 comprises coal gangue pyrolysis installation 6, water-gas reaction device 7, and the concrete structure of coal gangue pyrolysis installation 6, water-gas reaction device 7, raw gas take-up gear 8 is shown in the above, enter furnace charge storehouse 92 and be arranged on body of heater 91 top, body of heater 91 top is provided with into stove cloth passage 921, enter stove cloth passage 921 upper end and enter furnace charge storehouse 92 and communicate, enter stove cloth passage 921 lower end to communicate with pyrolysis vaporizer 61 top of coal gangue pyrolysis installation 6, hinge cage sealing discharging device 96 is arranged on bottom the inner ring cavity 758 of the annular hollow metal box body 755 of the steam generation device 75 of water-gas reaction device 7, product feed bin 94 is placed in bottom body of heater 91, product feed bin 94 connects hinge cage sealing discharging device 96, hinge cage sealing discharging device 96 belongs to prior art, as the sealing discharging device on market, sealing material returning device, sealing blanking device etc.
The method of this routine continuous pyrolysis gasification is:
(1), by the as-fired coal spoil pellet after controlling as-fired coal spoil rotary conveyor 95 damping being dewatered send in furnace charge storehouse 92, then pass through stove cloth passage 921 and enter in the pyrolysis vaporizer 61 of coal gangue pyrolysis installation 6;
(2), by gas-fired after purification in the outer gas-operated thermal bath facility 64 of coal gangue pyrolysis installation 6, interior gas-operated thermal bath facility 67 provide thermal source to pyrolysis vaporizer 61, coal gangue carries out pyrolysis under hot environment in pyrolysis vaporizer 61;
(3), high-temperature water vapor is passed into by water-gas reaction device 7 from pyrolysis vaporizer 61 bottom, and the coal gangue pyrolysis material hot with the high temperature of pyrolysis vaporizer 61 contacts, the charcoal in the solid product after coal gangue pyrolysis and superheated vapour meet and carry out water-gas reaction and generate water-gas;
(4), solid product after coal gangue pyrolytic gasification falls into high temperature reduction chamber 701 and the low temperature cooling chamber 702 of material heat sink 70 from pyrolysis vaporizer 61, overheated high-temperature water vapor is heated as again to the water vapor upwards entering pyrolysis vaporizer 61 through low temperature cooling chamber 702 and high temperature reduction chamber 701, again the solid product after coal gangue pyrolytic gasification is lowered the temperature simultaneously, in recycling low temperature cooling chamber 702, solid product waste heat adds thermosetting water vapor to the water in the body of heater water bag 753 of the annular hollow metal box body 755 of steam generation device 75, water vapor enters in steam pockets 754 by drum input tube 751, to supplementing a large amount of water vapors consumed because of water-gas reaction in steam pockets 754,
(5), steam pockets 754 enters siphunculus 707 by drum input tube 752 and steam and passes into water vapor to the low temperature cooling chamber 702 of material heat sink 70 again, and water-gas reaction can uninterruptedly be carried out continuously;
(6), the gas that produces in high temperature pyrolysis process of coal gangue and carry out water-gas reaction and generate water-gas (carbon monoxide and hydrogen), be referred to as raw gas, raw gas is derived by the raw gas take-up gear 8 that body of heater is arranged, to carry out recovery of chemical products and utilization, derivation main channel 84 process that simultaneously raw gas of comparatively high temps enters raw gas take-up gear from pyrolysis vaporizer 61 top carries out preheating to from the coal gangue pellet just entering stove entering pyrolysis vaporizer 61 top that stove cloth passage 921 enters again;
(7) according to coal gangue pyrolytic gasification degree, reed time controll hinge cage sealing discharging device 96 opens or cuts out, and is entered in product feed bin by the solid product after coal gangue high temperature pyrolysis and gasification cooling in low temperature cooling chamber 702 and inner ring cavity 758.
This example by coal gangue pyrolytic gasification process integration at the hot body of heater of same coal, realize continuous coal gangue pyrolytic gasification, production efficiency is high, needed for equipment, factory building face is little, human cost is low, utilize waste heat in the solid product after pyrolytic gasification to produce water vapor, the high humidity superheated vapour utilizing again water vapor to carry out lowering the temperature simultaneously required for generation water-gas reaction to the solid product after high temperature pyrolysis and gasification, has the feature of low consumption, environmental protection simultaneously.
The comprehensive cyclic utilization of Part IV, pyrolysis of coal gas
Chapter 1, the reclaiming clean of raw gas utilizes (change and produce)
First segment raw gas condensing works
Coal gangue pyrolytic gasification discharge raw gas temperature is higher, carries before recovery of chemical products for the ease of high temperature raw gas, sprays ammoniacal liquor cool high temperature raw gas.
The reclaiming clean of second section raw gas
Raw gas after ammoniacal liquor sprays carries out gas-liquid separation, other auxiliary product is refined containing multiple useful organic component such as carbolic oil, naphtalene oil, washing oil, carbolineum etc. for industry in mixed solution after gas-liquid separation, coal gas after gas-liquid separation is after air cooling cooling, after Dry recovery Recovery Purifying, become purified gas, purified gas can store for burning.
Chapter 2, raw gas reclaiming clean afterfire utilizes
Purified gas burning after first segment raw gas reclaiming clean
Purified gas after absorption is used for burning provides thermal source to coal gangue pyrolytic gasification.
Second section utilizes purified gas exhaust gases after combustion to saturated active coke regeneration heating
Hot waste gas after purified gas burning is used for because adsorption cleaning raw gas forms saturated active coke that to carry out evaporation thermal regeneration be unsaturated activated coke.
Section three, utilize purified gas to burn rear hot waste gas to the damping of as-fired coal spoil pellet
Hot waste gas after purified gas burning is used for carrying out damping dehydration to the coal gangue pellet entering stokehold.
Section three, utilize purified gas to burn rear hot waste gas to the damping of as-fired coal spoil pellet
Comprehensive above content draws a kind of coal gangue pyrolytic gasification raw gas combustion heat waste gas humidity control device and method, this device mainly comprises coal gangue pyrolysis gasifying device 93, raw gas take-up gear 8, as-fired coal spoil hot waste gas damping dewatering unit 1, concrete structure is shown in the above, here repeat no more, at this moment only explain with regard to its annexation.
As shown in figure 24, the exhaust gas fan 666 of the gas reversing system 66 of coal gangue pyrolysis installation 6 is connected by pipeline with the hot waste gas admission passage 131 of as-fired coal spoil hot waste gas damping dewatering unit 1.
Increase by a step in addition again after the 6th step after above-mentioned supplementing, exhaust gases after combustion in outer for coal gangue pyrolysis installation 6 gas-operated thermal bath facility 64, interior gas-operated thermal bath facility 67 is entered the hot waste gas admission passage 131 of as-fired coal spoil hot waste gas damping dewatering unit 1 by the exhaust gas fan 666 of gas reversing system 66, damping dehydration is carried out to as-fired coal spoil pellet.
Chapter 3, thermal cycling continuous coal gangue pyrolytic gasification is comprehensive
The continuous coal gangue pyrolytic gasification of first segment thermal cycling and damping and exhaust gas cleaner and method
Comprehensive above content draws a kind of thermal cycling continuous coal gangue pyrolytic gasification damping and exhaust gas cleaner and method, as shown in figure 24, this device comprises coal gangue pyrolytic gasification stove 9, and as-fired coal spoil rotary conveyor 95, as-fired coal spoil bucket elevator 18, discharge transfer roller 15, as-fired coal spoil hot waste gas damping dewatering unit 1, tail gas water wash one's hair cleaner 16, infeed belt conveyor 17; Wherein coal gangue pyrolytic gasification stove 9 comprise body of heater 91, enter furnace charge storehouse 92, coal gangue pyrolysis gasifying device 93, raw gas take-up gear 8, hinge cage sealing discharging device 96, product feed bin 94, concrete structure is shown in the above, repeats no more here; Wherein as-fired coal spoil rotary conveyor 95, as-fired coal spoil bucket elevator 18, discharge transfer roller 15, infeed belt conveyor 17 are the universal product on market, and concrete structure also repeats no more here, only explains with regard to their annexation here.
As shown in figure 23, as-fired coal spoil rotary conveyor 95, as-fired coal spoil bucket elevator 18, discharge transfer roller 15, infeed belt conveyor 17, hinge cage sealing discharging device 96 are connected with industry control center 90, are automatically controlled the work of as-fired coal spoil rotary conveyor 95, as-fired coal spoil bucket elevator 18, discharge transfer roller 15, infeed belt conveyor 17, hinge cage sealing discharging device 96 by industry control center 90.
As shown in figure 24, infeed belt conveyor 17 is arranged on opening for feed 112 place of as-fired coal spoil hot waste gas damping dewatering unit 1, discharge transfer roller 15 1 end is connected on bottom blanking bin 14, discharge transfer roller 15 the other end is connected on bottom as-fired coal spoil bucket elevator 18, as-fired coal spoil bucket elevator 18 top access stove coal gangue rotary conveyor 95, as-fired coal spoil rotary conveyor 95 is connected on into furnace charge storehouse 92, second gas conveying tube (figure is not depending on illustrating) of the activated coke Dry recovery device that the raw gas export mouth 851 of raw gas take-up gear 8 can connect, also other raw gas refining plants on market can be connect, as long as the coal gas after purification is connected with the gas fan 665 of gas reversing system 66 by pipeline, exhaust gas fan 666 is connected with the hot waste gas admission passage 131 of as-fired coal spoil hot waste gas damping dewatering unit 1, the tail gas that the external exhaust fan 137 (shown in Fig. 1) of the low temperature waste gas relief outlet 138 of as-fired coal spoil hot waste gas damping dewatering unit 1 and tail gas water wash one's hair cleaner 16 enters pipe 169 and connects.
The thermal cycling continuous coal gangue pyrolytic gasification damping of this example and exhaust purifying method are:
(1), the common coal gangue pellet after pulverizing is sent in as-fired coal spoil hot waste gas damping dewatering unit 1 and is carried out damping dehydration by infeed belt conveyor 17;
(2) the as-fired coal spoil pellet, after damping dehydration is sent into coal gangue pyrolytic gasification stove 9 carried out the gasification of high temperature continuous pyrolysis by discharge transfer roller 15, as-fired coal spoil bucket elevator 18, as-fired coal spoil rotary conveyor 95;
(3) solid product, after pyrolytic gasification enters product feed bin 94, and the raw gas produced in pyrolytic gasification is sent in the coal gangue pyrolysis installation 6 of coal gangue pyrolytic gasification stove 9 through purification and carried out gas two and enter a regenerative heat exchange mode out and burn and provide thermal source to coal gangue pyrolytic gasification;
(4), the hot waste gas after burning is sent in as-fired coal spoil hot waste gas damping dewatering unit 1 by exhaust gas fan 666 and hot waste gas admission passage 131, utilize the waste heat of hot waste gas to provide thermal source to the damping of the coal gangue pellet after pulverizing dehydration, lower the temperature to hot waste gas again simultaneously;
(5), the hot waste gas after cooling is entered pipe 169 by exhaust fan 137 and tail gas send into tail gas water and wash one's hair in cleaner 16 and carry out water and wash one's hair purifying and dedusting and again lower the temperature, finally obtain ordinary temp and clean waste gas discharges in air.
Second section thermal cycling continuous coal gangue pyrolytic gasification composite technology
Comprehensive above content draws the composite technology that a kind of thermal cycling continuous coal gangue pyrolytic gasification is complete, includes stove coal gangue hot waste gas damping dehydration, coal gangue pyrolytic gasification, raw gas condensation, raw gas reclaiming clean, tail gas water washes one's hair purification etc.
Section three, the control of thermal cycling continuous coal gangue pyrolytic gasification composite technology
The various electrical equipments used in the technique such as UTILIZATION OF VESIDUAL HEAT IN of the present invention by the hot waste gas after coal gangue pyrolytic gasification, raw gas reclaiming clean, purified gas burning, burning are controlled, and make thermal cycling continuous coal gangue pyrolytic gasification smooth.
Above content introduction just exemplifies a tool embodiment of thermal cycling continuous coal gangue pyrolytic gasification integration unit and technique, does not form the restriction to this case thermal cycling continuous coal gangue pyrolytic gasification integration unit and technique protection domain.

Claims (10)

1. thermal cycling continuous coal gangue pyrolytic gasification damping and exhaust gas cleaner, is characterized in that: the coal gangue pyrolysis gasifying device and raw gas take-up gear, as-fired coal spoil hot waste gas damping dewatering unit, the tail gas water that mainly comprise coal gangue pyrolytic gasification stove wash one's hair cleaner, described coal gangue pyrolysis gasifying device mainly comprises coal gangue pyrolysis installation and water-gas reaction device, described coal gangue pyrolysis installation is arranged in the middle part of body of heater, mainly comprise pyrolysis vaporizer, outer gas-operated thermal bath facility, interior gas-operated thermal bath facility, central supported bow, described pyrolysis vaporizer forms an annulus by the inside and outside ringwall of fire-resistant thermally conductive material, being centered around pyrolysis vaporizer's outer ring wall periphery is outer gas-operated thermal bath facility, is interior gas-operated thermal bath facility in ringwall ring in pyrolysis vaporizer, described water-gas reaction device comprises pyrolysis vaporizer, material heat sink, steam generation device, the pyrolysis vaporizer of described pyrolysis vaporizer and coal gangue pyrolysis installation is same room, pyrolysis vaporizer is positioned at central supported bow top, described material heat sink, steam generation device is positioned at central supported bow below, described material heat sink comprises high temperature reduction chamber, low temperature cooling chamber, reduction chamber bridge arch, the top of high temperature reduction chamber communicates with bottom pyrolysis vaporizer, high temperature reduction chamber and low temperature cooling chamber setting up and down, reduction chamber bridge arch is arranged between high temperature reduction chamber and low temperature cooling chamber, described reduction chamber bridge arch comprises bridge bow, steam chest, steam enters siphunculus, bridge bow middle part forms steam chest, the lower openings of steam chest is towards low temperature cooling chamber, steam enters siphunculus and is arranged in bridge bow, steam enters siphunculus one end and leads to steam chest, the other end stretches out outside stove, described steam generation device comprises annular hollow metal box body, steam pockets and drum input tube, drum output tube, annular hollow metal box body is arranged on bottom of furnace body, the inner ring cavity of annular hollow metal box body is connected to the low temperature cooling chamber bottom of material heat sink, the body of heater water bag that opposing seal is used for storage of water is formed in annular hollow metal box body case, body of heater water bag is connected to water inlet pipe and drum input tube, water inlet pipe communicates with water tank, drum input tube and steam pockets are connected, drum output tube and the steam of material heat sink of steam pockets enter that one end that siphunculus stretches out outside stove and communicate, described raw gas take-up gear comprises raw gas concentration chamber, interior derivation passage, outer derivation passage, derive main channel, derive circuit, described raw gas concentration chamber be arranged on the top of pyrolysis vaporizer and pyrolysis vaporizer integrally formed, interior derivation channel setting is in internal-quirk partition wall, interior derivation feeder connection leads to pyrolysis vaporizer through in the middle part of interior ringwall, interior derivation channel outlet leads to the raw gas concentration chamber at pyrolysis vaporizer top through interior ringwall, in the exterior wall of described outer derivation channel setting body of heater, lower outside derivation feeder connection, upper outside derivation feeder connection leads to pyrolysis vaporizer through in the middle part of outer ring wall, outer derivation channel outlet leads to the raw gas concentration chamber at pyrolysis vaporizer top through outer ring wall, described derivation main channel is arranged in the exterior wall of the body of heater of coal gangue pyrolytic gasification stove, derive main channel inlets communicate with raw gas concentration chamber extend up to the exterior wall top being arranged on body of heater again derivation circuit in, derive circuit and be provided with raw gas export mouth, described as-fired coal spoil hot waste gas damping dewatering unit mainly comprises housing, steam steam discharge exporter, waste gas heat exchange dehydrator, blanking bin, form feed bin in described housing, feed bin relative closure top is only provided with opening for feed, and described blanking bin is arranged on housing bottom and communicates with feed bin, described steam steam discharge exporter comprises steam derives house steward, more than at least one steam derives umbrella road, vapor collection standpipe, water of condensation discharge manifold, it is umbrella shape inclination bending member that steam derives umbrella road, and many steam are derived umbrella road and are regularly horizontally installed in feed bin in interval, vapor collection standpipe is longitudinally arranged in the relative both sidewalls of housing, and steam is derived two ends, umbrella road and is separately fixed on both sidewalls vapor collection standpipe, bending member curved recessed in vapor collection standpipe on be provided with steam export mouth, steam is derived house steward and is arranged in the sidewall of the upper shell of vapor collection standpipe, steam is derived house steward and is communicated with vapor collection riser upper, steam is derived house steward and is also provided with water vapor relief outlet, water of condensation discharge manifold is arranged in the sidewall of below housing of vapor collection standpipe, water of condensation discharge manifold communicates with vapor collection standpipe bottom, and water of condensation discharge manifold is also provided with condensed water discharge outlet, described waste gas heat exchange dehydrator comprises hot waste gas admission passage, hot waste gas enters room, radiating pipe, radiating pipe serial connection passage, waste gas transition chamber, low temperature waste gas discharge chamber, the hot waste gas room of entering is arranged in middle and upper part one sidewall of housing, what waste gas transition chamber was arranged on housing enters in the relative another side sidewall in room with hot waste gas, low temperature waste gas discharge chamber is arranged on the bottom of housing and hot waste gas enters in the same face sidewall of room, and low temperature waste gas discharge chamber is provided with low temperature waste gas relief outlet, several radiating pipes serial connection passage parallel internal bin passing across housing between two, be connected on hot waste gas to enter between room and waste gas transition chamber and between waste gas transition chamber and low temperature waste gas discharge chamber, one end of upper radiating pipe serial connection passage communicates with the hot waste gas room of entering and the other end is closed, and one end of next radiating pipe serial connection passage is closed and the other end communicates with waste gas transition chamber, in like manner, between waste gas transition chamber and low temperature waste gas discharge chamber, also be that one end of upper radiating pipe serial connection passage communicates with waste gas transition chamber and the other end is closed, one end of next radiating pipe serial connection passage is closed and the other end communicates with low temperature waste gas discharge chamber, the rest may be inferred, several radiating pipes also adopt metallic substance to make, several radiating pipes are spaced on radiating pipe serial connection passage, radiating pipe one end is connected on parallel upper radiating pipe serial connection passage, the other end be connected on parallel next radiating pipe serial connection passage on, by mutually through for radiating pipe parallel between two serial connection passage, room is entered and waste gas transition chamber is connected by hot waste gas, waste gas transition chamber and low temperature waste gas discharge chamber are connected, described tail gas water is washed one's hair cleaner and is comprised purification cylindrical shell, atomized spray, stainless steel filter wire stratum reticulare, tail gas pod, tank, water reservoir, sprinkling water pump, described purification cylindrical shell top arranges exhaust port, described atomized spray, stainless steel filtration silk screen, tail gas pod, tank all arrange in purification cylindrical shell, described water reservoir, spraying water pump, all to arrange purifying tube external, described tank arranges the bottom of purification cylindrical shell, and bottom of gullet is provided with spoil disposal pipeline, described tail gas pod is the top that the cylindrical cover of a lower ending opening upper end closed is arranged on tank, and tail gas water conservancy diversion is covered with a tail gas and enters pipe, and tail gas enters pipe and passes purification cylindrical shell and communicate with the external world, stainless steel filter wire stratum reticulare is provided with above tail gas pod, stainless steel filter wire stratum reticulare periphery is completely fixed on purifying tube body wall face, above stainless steel filter wire stratum reticulare, atomized spray is set, atomized spray is connected on water inlet pipe, water inlet pipe is connected with sprinkling water pump by water inlet supervisor, spray water pump and be connected to water absorption tube, water absorption tube stretches in water reservoir, water reservoir is also communicated with tank through purification cylindrical shell by communicating pipe, the raw gas of discharging from raw gas export mouth is purified, the outer gas-operated thermal bath facility of coal gangue pyrolysis installation delivered to again by raw gas after purification, interior gas-operated thermal bath facility burns, waste gas after burning delivers to the hot waste gas admission passage of the waste gas heat exchange dehydrator of as-fired coal spoil hot waste gas damping dewatering unit again by pipeline, the tail gas that the low temperature waste gas relief outlet of waste gas heat exchange dehydrator and tail gas water wash one's hair cleaner is entered pipe and connected by pipeline.
2. thermal cycling continuous coal gangue pyrolytic gasification damping as claimed in claim 1 and exhaust gas cleaner, it is characterized in that: described coal gangue pyrolysis installation also comprises gas reversing system, described outer gas-operated thermal bath facility is mainly some groups of structure identical association first combustion heaters, second combustion heater is formed, the first described combustion heater mainly comprises the first combustion chamber, first coal gas enters arm and the first regenerative heat exchanger, first coal gas enters arm and leads in the first combustion chamber through body of heater exterior wall, the body of heater exterior wall that first combustion chamber is made up of refractory materials and fire-resistant thermally conductive material make the gas-fired quirk that pyrolysis vaporizer's outer ring wall and outer quirk partition wall surround a relative closure, the first described regenerative heat exchanger comprises the first thermal, first heat storage, first air enters arm and the first combustion exhaust exhaust outlet, first thermal is arranged in body of heater exterior wall, first heat storage arranges in the first thermal, the first bottom of combustion chamber is led in first thermal one end, the other end is connected to the first air respectively and enters arm and the first combustion exhaust exhaust outlet, in like manner identical second combustion heater of structure also mainly comprises the second combustion chamber, second coal gas enters arm and the second regenerative heat exchanger, between the first described combustion chamber and second combustion chamber of next-door neighbour, outer quirk is provided with combustion chamber through hole every coping, first combustion chamber is connected to form with second combustion chamber of next-door neighbour and is associated one group by combustion chamber through hole, described interior gas-operated thermal bath facility is primarily of identical association the 3rd combustion heater of some groups of structures, 4th combustion heater, its structure with associate the first burning heater, second burning heater composition is almost identical, the 3rd combustion chamber unlike the 3rd combustion heater is made ringwall and internal-quirk partition wall in pyrolysis vaporizer by fire-resistant thermally conductive material and is surrounded the gas-fired quirk of a relative closure, 3rd coal gas enters passing beneath and upwards leading to the 3rd combustion chamber of article bow that arm bends from central supported, 3rd thermal is arranged on article body of heater of bow below, 3rd heat storage is placed in the 3rd thermal, the 3rd bottom of combustion chamber is led in the upwards extension that passes beneath of article bow that the 3rd thermal one end is bent from central supported by extension passage, the 3rd thermal the other end is connected to the 3rd air respectively and enters arm and the 3rd combustion exhaust exhaust outlet, between the 3rd described combustion chamber and the 4th combustion chamber of next-door neighbour, internal-quirk is provided with chamber passage every coping, 3rd combustion chamber is connected to form with the 4th combustion chamber of next-door neighbour and is associated one group by chamber passage, described gas reversing system comprises dish, lower wall, rotate reversing motor, air blower, gas fan, exhaust gas fan, lower wall is connected to an air supervisor respectively and the first air is in charge of, second air is in charge of, a coal gas supervisor and the first gas manifold, second gas manifold, a combustion exhaust supervisor and the second combustion exhaust are in charge of, first combustion exhaust is in charge of, wherein the second combustion exhaust is in charge of to be in charge of with the first combustion exhaust to be in charge of with the first air and is in charge of with the second air and the setting of the first gas manifold and the second gas manifold is just exchanged, upper dish is fitted in above lower wall, upper dish respectively correspondence is provided with air pipe connecting, gas connection pipes, combustion exhaust pipe connecting, rotate reversing motor and drive upper dish reciprocating rotation thus realize air supervisor and be constantly in charge of with the first air to be in charge of with the second air and carry out connecting and cutting off conversion on lower wall, coal gas supervisor constantly carries out connecting and cutting off conversion with the first gas manifold and the second gas manifold, combustion exhaust supervisor is constantly in charge of with the second combustion exhaust to be in charge of with the first combustion exhaust and carries out connecting and cutting off conversion, wherein, the first described air be in charge of enter arm with the first air, the 3rd air enter arm connect, simultaneously, the first described gas manifold and the first coal gas enter arm, the 3rd coal gas enters arm and connects, simultaneously now, the first described combustion exhaust is in charge of and is connected with the first combustion exhaust exhaust outlet, the 3rd combustion exhaust exhaust outlet, in like manner, second air be in charge of enter arm with the second air, the 4th air enter arm connect, simultaneously, second gas manifold and the second coal gas enter arm, the 4th coal gas enters arm and connects, meanwhile, the second combustion exhaust is in charge of and is connected with the second combustion exhaust exhaust outlet, the 4th combustion exhaust exhaust outlet.
3. thermal cycling continuous coal gangue pyrolytic gasification damping as claimed in claim 2 and exhaust gas cleaner, it is characterized in that: described coal gangue pyrolysis installation also comprises the periphery that two groups of bustle pipes are arranged on body of heater, comprise the first air bustle pipe, the first coal gas bustle pipe, the first combustion exhaust bustle pipe; Second air bustle pipe, the second coal gas bustle pipe, the second combustion exhaust bustle pipe; The first wherein said air be in charge of enter arm by the first air bustle pipe and the first air, the 3rd air enter arm connect, simultaneously, the first described gas manifold enters arm by the first coal gas bustle pipe and the first coal gas, the 3rd coal gas enters arm and connects, simultaneously now, the first described combustion exhaust is in charge of and is connected with the first combustion exhaust exhaust outlet, the 3rd combustion exhaust exhaust outlet by the first combustion exhaust bustle pipe; In like manner, second air be in charge of enter arm by the second air bustle pipe and the second air, the 4th air enter arm connect, simultaneously, second gas manifold enters arm by the second coal gas bustle pipe and the second coal gas, the 4th coal gas enters arm and connects, meanwhile, the second combustion exhaust is in charge of and is connected with the second combustion exhaust exhaust outlet, the 4th combustion exhaust exhaust outlet by the second combustion exhaust bustle pipe.
4. thermal cycling continuous coal gangue pyrolytic gasification damping as claimed in claim 2 and exhaust gas cleaner, is characterized in that: the exhaust gas fan of the gas reversing system of described coal gangue pyrolysis installation and the hot waste gas admission passage of as-fired coal spoil hot waste gas damping dewatering unit are connected by pipeline.
5. thermal cycling continuous coal gangue pyrolytic gasification damping as claimed in claim 1 and exhaust gas cleaner, it is characterized in that: described outer gas-operated thermal bath facility is mainly divided into the heating of upper, middle and lower segment formula, and every section is made up of 9 groups of identical first combustion heaters of structure, second combustion heaters.
6. thermal cycling continuous coal gangue pyrolytic gasification damping as claimed in claim 1 and exhaust gas cleaner, it is characterized in that: described interior gas-operated thermal bath facility is mainly divided into the heating of upper and lower two-section type, and every section is made up of 6 groups of identical 3rd combustion heaters of structure, the 4th combustion heaters.
7. thermal cycling continuous coal gangue pyrolytic gasification damping as claimed in claim 1 and exhaust gas cleaner, it is characterized in that: the radiating pipe of described waste gas heat exchange dehydrator is in " U " type, the arrangement in two rows on radiating pipe serial connection passage of U-shaped radiating pipe, the U-shaped radiating pipe of a upper row is inverted U, and the U-shaped mouth of the U-shaped radiating pipe of a upper row is relative with the U-shaped mouth of the U-shaped radiating pipe of next row.
8. thermal cycling continuous coal gangue pyrolytic gasification damping as claimed in claim 1 and exhaust gas cleaner, it is characterized in that: the external exhaust fan of low temperature waste gas relief outlet of described waste gas heat exchange dehydrator, exhaust fan washes one's hair cleaner again tail gas with tail gas water enters pipe and connects.
9. thermal cycling continuous coal gangue pyrolytic gasification damping as claimed in claim 1 and exhaust gas cleaner, it is characterized in that: the purifying tube body wall face above described tank offers water-in, and the condensed water discharge outlet of the water of condensation discharge manifold of water-in and steam steam discharge exporter is connected by pipeline.
10. thermal cycling continuous coal gangue pyrolytic gasification damping as claimed in claim 1 and exhaust gas cleaner, it is characterized in that: described atomized spray, stainless steel filter wire stratum reticulare in purification cylindrical shell from bottom to top interval arrange many groups, the order number of the one group of stainless steel filter wire stratum reticulare in top is greater than the order number of the one group of stainless steel filter wire stratum reticulare in below.
CN201310121735.5A 2013-04-10 2013-04-10 Continuous thermal cycle coal gangue pyrolysis gasification humidifying and tail gas purifying device Active CN103242908B (en)

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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN202482249U (en) * 2011-12-21 2012-10-10 山西鑫立能源科技有限公司 Coal pyrolysis furnace
CN202808699U (en) * 2012-09-21 2013-03-20 山西鑫立能源科技有限公司 Low metamorphic soft coal pyrolyzing furnace
CN203229498U (en) * 2013-04-10 2013-10-09 山西鑫立能源科技有限公司 Thermal cycle continuous coal gangue pyrolysis gasification humidity control and tail gas purifying device

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN202482249U (en) * 2011-12-21 2012-10-10 山西鑫立能源科技有限公司 Coal pyrolysis furnace
CN202808699U (en) * 2012-09-21 2013-03-20 山西鑫立能源科技有限公司 Low metamorphic soft coal pyrolyzing furnace
CN203229498U (en) * 2013-04-10 2013-10-09 山西鑫立能源科技有限公司 Thermal cycle continuous coal gangue pyrolysis gasification humidity control and tail gas purifying device

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