CN103937521A - External heating vertical overturn dumping pyrolyzing furnace - Google Patents
External heating vertical overturn dumping pyrolyzing furnace Download PDFInfo
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- CN103937521A CN103937521A CN201410190452.0A CN201410190452A CN103937521A CN 103937521 A CN103937521 A CN 103937521A CN 201410190452 A CN201410190452 A CN 201410190452A CN 103937521 A CN103937521 A CN 103937521A
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Abstract
The invention discloses an external heating vertical overturn dumping pyrolyzing furnace and belongs to the field of the pyrolyzing equipment. The pyrolyzing furnace comprises a furnace body, a feeding device, a dry distillation gas collecting pipe, a gas supply pipe, a cooking tank, and a spiral discharging device; a plurality of dry distillation chambers and a plurality of combustion chambers are vertically arranged in the furnace body, the dry distillation chambers are arranged alternately with the combustion chambers, and not intercommunicated with the combustion chamber, and a vertical corrugated fuel falling channel is arranged in each dry distillation chamber; the feeding device is arranged at the upper end of the furnace body and communicated with the upper end openings of the plurality of dry distillation chambers in the furnace body; the dry distillation gas collecting pipe is arranged on the furnace body and communicated with the plurality of dry distillation chambers in the furnace body; the gas supply pipe is arranged on the furnace body and communicated with the plurality of combustion chambers in the furnace body, respectively; the cooling tank is arranged at the bottom of the furnace body; the spiral discharging device is arranged in the cooling tank and communicated with the lower end openings of the dry distillation chambers in the furnace body. The pyrolyzing furnace is simple in structure and high in efficiency, and further is capable of effectively pyrolyzing solid fossil fuels having the granularity of lower than 30mm.
Description
Technical field
The present invention relates to the pyrolysis plant field of solid fossil fuel, particularly relate to a kind of outer hot vertical tilting pyrolysis oven of pyrolysis solid fossil fuel.
Background technology
At present; with the method production cleaning of pyrolysis or the fuel of upgrading; both can reduce the environmental pollution that direct burning solid fossil oil causes; can make full use of the compound of high economic worth contained in solid fossil fuel again, there is protection of the environment, energy-conservation and rationally utilize the broad sense of solid fossil resource.
And according to the difference of pyrolytic process, the pyrolysis oven adopting has internal thermal upright stove and external-heat upright furnace, external-heat upright furnace technique be wherein nineteen fifties in the method for Britain, German widely used production city coal gas and semicoke, main technique has hot vertical heater etc. outside Wood (W-D) charring furnace, Kao Baisi (Koppers) Lu He China Inner Mongol Yi Dong group.The groundwork principle of external-heat upright furnace is: the upright thin-and-long structure of laying fireproof bricks for destructive distillation chamber, coal enters into indoor straight-through decline the continuously of heated destructive distillation from top coal bunker through suitably constructing, coal is heated and pyrolysis gradually by showing tremendous enthusiasm road in folding process, the speed that coal moves down starts by pyrolysis and reaches destructive distillation chamber bottom to become the coke time and control with coal, and the byproducts such as raw gas that in pyrolytic process, coal discharges gradually rise to top, destructive distillation chamber and are exported.
At least there is following shortcoming in existing external-heat upright furnace: because destructive distillation chamber is upright thin-and-long structure, heated solid materials is indoor straight-through decline the continuously of destructive distillation, if solid material granularity is less than 10mm, there is the closely knit filling destructive distillation of the solid materials interior space, the easy adhesion of material in pyrolytic process, and do not have or rare space, and then cause byproducts such as pyrolysis gas that in pyrolytic process, fossil oil discharges to be gradually difficult for rising to top, destructive distillation chamber being exported, therefore the small particle size solid fossil fuel that existing external-heat upright furnace can not be less than 10mm to granularity is carried out effective pyrolysis.
Summary of the invention
The technical problem to be solved in the present invention is to provide a kind of outer hot vertical tilting pyrolysis oven, its raw material is applied widely, the non-caked material of solid all can be used, and can conveniently control the dust producing in small particle size raw material pyrolytic process, thereby solve the problem that external-heat pyrolysis stove can not effectively pyrolysis granularity be less than the small particle size solid fossil fuel of 10mm.
For solving the problems of the technologies described above, the invention provides a kind of outer hot vertical tilting pyrolysis oven, comprising:
Body of heater, is vertically provided with some destructive distillation chamber and some combustion chambers in it, described destructive distillation chamber and interval, described combustion chamber arrange, and described destructive distillation chamber is not communicated with mutually with described combustion chamber; The indoor fuel decline passway that is equipped with vertical setback shape of described each destructive distillation;
Feeding unit, is arranged on described body of heater upper end, is communicated with the upper end open of some destructive distillation chamber in described body of heater;
Carbonization gas collection tube, is arranged on described body of heater, is communicated with respectively with the some destructive distillation chamber in described body of heater;
Gaspipe, is arranged on described body of heater, is communicated with respectively with the some combustion chambers in described body of heater;
Cooling tank, is arranged on described bottom of furnace body;
Spiral discharging device, is arranged in described cooling tank, is communicated with the lower ending opening of destructive distillation chamber in described body of heater.
Beneficial effect of the present invention is: by the indoor fuel decline passway that vertical setback shape is all set of each destructive distillation, make to be declined in the mode of setback (the direction upset that is equivalent to decline after one section of every decline changes) by the solid fossil fuel of pyrolysis, and can form space at the bending part of fuel decline passway, like this when solid fossil fuel particle diameter hour, can be because not piling up in the indoor straight-through decline of destructive distillation, can when pyrolysis, not bond, the rising that does not affect the byproducts such as coal gas after pyrolysis is collected, and does not also affect the discharge of flue gas.This pyrolysis oven is simple in structure, and efficiency is high, and the small particle size solid fossil fuel that can be effectively granularity be less than to 10mm is carried out pyrolysis.
Accompanying drawing explanation
In order to be illustrated more clearly in the technical scheme of the embodiment of the present invention, below the accompanying drawing of required use during embodiment is described is briefly described, apparently, accompanying drawing in the following describes is only some embodiments of the present invention, for those of ordinary skill in the art, do not paying under the prerequisite of creative work, can also obtain other accompanying drawings according to these accompanying drawings.
The external structure schematic diagram of the pyrolysis oven that Fig. 1 provides for the embodiment of the present invention;
The side structure schematic diagram of the pyrolysis oven that Fig. 2 provides for the embodiment of the present invention;
Fig. 3 cuts open schematic diagram for the bowing of body of heater of the pyrolysis oven that the embodiment of the present invention provides;
The side of the body of heater of the pyrolysis oven that Fig. 4 provides for the embodiment of the present invention is cutd open schematic diagram;
Structural representation in the body of heater of the pyrolysis oven that Fig. 5 provides for the embodiment of the present invention;
The structural representation of the destructive distillation chamber in the body of heater of the pyrolysis oven that Fig. 6 provides for the embodiment of the present invention;
The pyrolysis oven that Fig. 7 provides for the embodiment of the present invention from furnace roof vertical section gained combustion chamber flue schematic diagram.
Embodiment
Below the technical scheme in the embodiment of the present invention is clearly and completely described, obviously, described embodiment is only the present invention's part embodiment, rather than whole embodiment.Based on embodiments of the invention, those of ordinary skills, not making the every other embodiment obtaining under creative work prerequisite, belong to protection scope of the present invention.
Fig. 1,2 is depicted as a kind of outer hot vertical tilting pyrolysis oven that the embodiment of the present invention provides, and for solid fossil fuel is carried out to pyrolysis, the small particle size solid fossil fuel that is specially adapted to the granularity to be less than 10mm is carried out pyrolysis, and this pyrolysis oven comprises:
Body of heater 1, is vertically provided with some destructive distillation chamber 6 and some combustion chambers 7 in it, destructive distillation chamber 6 arranges (referring to Fig. 3) with 7 intervals, combustion chamber, and destructive distillation chamber 6 is not communicated with mutually with combustion chamber 7; In each destructive distillation chamber 6, be equipped with the fuel decline passway 32 of vertical setback shape;
Feeding unit 9, is arranged on body of heater 1 upper end, is communicated with the upper end open of some destructive distillation chamber 6 in body of heater 1;
Carbonization gas collection tube 4, is arranged on body of heater 1, is communicated with respectively with the some destructive distillation chamber 6 in body of heater 1;
Gaspipe 5, is arranged on body of heater 1, is communicated with respectively with the some combustion chambers 7 in body of heater 1;
Cooling tank 10, is arranged on body of heater 1 bottom;
Spiral discharging device 8, is arranged in cooling tank 10, is communicated with the lower ending opening of destructive distillation chamber 6 in body of heater 1.
In above-mentioned pyrolysis oven, by at the indoor fuel decline passway that is equipped with vertical setback shape of each destructive distillation, while having avoided pyrolysis small particle size solid fossil fuel, the straight-through accumulation that declines and cause of fuel, not only avoided causing fuel bonding when pyrolysis, also can form space at fuel decline passway bending part, facilitate the rising of the coal gas that pyrolysis goes out to collect.Solved the problem that existing external-heat pyrolysis stove can not effectively pyrolysis small particle size solid fossil fuel.
As shown in Figure 2, in above-mentioned pyrolysis oven, the indoor fuel decline passway that is equipped with vertical setback shape of each destructive distillation is formed by following structure:
Some swash plates 3, are stratified and set on indoor two the relative inwalls of destructive distillation from top to bottom;
The strut member 31 that supports use is all set between each swash plate 3 and this swash plate place inwall;
In some swash plates 3, the swash plate upper end in odd-level is fixed on the indoor side inwall of destructive distillation, and the swash plate in even level is fixed on the opposite inwall of a side inwall;
Each swash plate lower end is to the free end of the indoor oblique below inclination of destructive distillation, keeps interval with opposite inwall, and keeps interval with the swash plate of this swash plate below;
The lower end of two neighbouring swash plates refers in the opposite direction;
In destructive distillation chamber 6, the plate face of each swash plate and each swash plate lower end are communicated with into the fuel decline passway 32 of vertical setback shape far from interval and each swash plate lower end of opposite inwall far from the interval of below swash plate from top to bottom.
The fuel decline passway that above-mentioned this structure forms, each Chu Wei space, swash plate rear, facilitates the coal gas rising after pyrolysis to collect.
In above-mentioned pyrolysis oven, body of heater 1 by the identical some pyrolysis unit stoves 11 of structure from top to bottom layering setting be formed by connecting (as shown in Figure 1); Each pyrolysis unit stove junction can adopt high temperature sealing material sealing, guarantees the whole destructive distillation chamber of formation and the stopping property of integral combustion chamber;
Wherein, be equipped with some destructive distillation chamber and some combustion chambers in each pyrolysis unit stove, destructive distillation chamber and interval, combustion chamber arrange, and destructive distillation chamber is not communicated with mutually with combustion chamber, and the structure of pyrolysis unit stove can be referring to Fig. 3 to Fig. 5;
In each pyrolysis unit stove, be equipped with swash plate and be supported on this swash plate and its place inwall between strut member, each swash plate lower end is the free end that tilts to the indoor oblique below of destructive distillation, keeps interval with opposite inwall;
Swash plate in neighbouring two pyrolysis unit stoves arranges towards the opposite;
Several whole destructive distillation chambers and several whole combustion chambers of after some pyrolysis unit stoves 11 connect, forming, the plate face of the swash plate in indoor each pyrolysis unit stove from top to bottom of each whole destructive distillation and each swash plate lower end are communicated with into the fuel decline passway of vertical setback shape far from interval and each swash plate lower end of opposite inwall far from the interval of below swash plate.
The body of heater that above-mentioned this mode forms, when the height of body of heater is higher, is divided into the more convenient construction of a plurality of pyrolysis unit stoves.
Above-mentioned pyrolysis oven also comprises: partition wall 2, be horizontally installed in body of heater 1, and be connected between the antetheca and rear wall in body of heater 1, the some destructive distillation chamber in body of heater 1 and some combustion chambers are divided into two portions.When body of heater size is larger, by being set, can guarantee on partition wall 2 steadiness of body of heater integral body like this.
In above-mentioned pyrolysis oven, carbonization gas collection tube 4 is two groups, divides the both sides that are located at body of heater 1;
Every group of carbonization gas collection tube forms with some take-off pipes that interval is connected on supervisor from top to bottom by supervisor, and each take-off pipe 41 is connected to the bending part of the fuel decline passway of the indoor vertical setback shape of destructive distillation.
In above-mentioned pyrolysis oven, gaspipe 5 is two groups, divides the both sides that are located at body of heater 1;
Every group of gaspipe 5 by main tracheae and the some minutes segmental bronchuses that interval is connected on main tracheae from top to bottom form, within each minute, segmental bronchus 51 is communicated with combustion chamber 7 is interior respectively.
In above-mentioned pyrolysis oven, body of heater 1 is rectangular structure, and the outer wall of body of heater is thermal insulation layer 10.Preferred thermal insulation layer 10 is three-decker, and wherein, internal layer is fire brick layer 101, and middle layer is asbestos layer 102, and skin is undercloak 103.
In above-mentioned pyrolysis oven, feeding unit 9 consists of trapezoidal hopper storage bin and the rotary pocket feeder that is arranged on trapezoidal hopper storage bin bottom, and the feed opening of rotary pocket feeder is communicated with the upper end open coupling of the destructive distillation chamber of body of heater.
In above-mentioned pyrolysis oven, inside, combustion chamber is provided with several lighting-up tuyeres, and the upper and lower edge of each lighting-up tuyere all arranges dividing plate, and each dividing plate and Inner Wall of Combustion Chamber form the rising passway of turning back of high-temperature flue gas smoke evacuation; Wherein, on each lighting-up tuyere, along dividing plate near-end, be adjacent to the sidewall at this lighting-up tuyere place, upper along dividing plate far-end and far-end sidewall maintenance 200mm distance; Under each lighting-up tuyere, along dividing plate and this lighting-up tuyere proximal, side wall, keep 200mm distance, along dividing plate far-end and far-end sidewall, be close to down; Each dividing plate forms the rising passway of turning back of discharging fume in combustion chamber, and (as shown in Figure 7, wherein, 5 is gaspipe; 10 is furnace wall; 511 is lighting-up tuyere; 71 is the dividing plate on upper edge; 72 is the dividing plate on lower edge; 73 rising passwaies of turning back for smoke evacuation).
Below in conjunction with the drawings and specific embodiments, pyrolysis oven of the present invention is described further.
Pyrolysis oven of the present invention carries out pyrolysis mainly for the non-caked material of solid, its pyrolysis principle is: pyrolysis material enters pyrolysis oven by upper of furnace body closed-type feed device, material directly contacts with pyrolysis furnace wall and inner swash plate, descending under self gravitation effect, the warm flue gas of height that absorbs combustion chamber gas-fired with thermal radiation, the direct mode contacting in descending process is passed to the heat of furnace wall, be elevated to gradually the temperature of setting, through super-dry, abundant pyrolysis, produce gas and solid grog.Suitable material bed of gas penetration thickness enters triangle air chamber under swash plate, in air chamber, gas accumulation to a certain extent, gaseous tension will be greater than the vertical effuser gaseous tension being attached thereto, under High Pressure, by plenum openings conduit, enter vertical collecting pipe, by pipeline, be transported to next workshop section; Descending solid materials becomes grog and enters spiral discharging device after abundant pyrolysis, carrying out indirect heat exchange with the water coolant of spiral discharging device outer wall lowers the temperature gradually, continue to be forwarded to the cooling water heat exchange cooling of cylinder water cooler and outer wall, when clinker temperature reach burning-point following after discharging, complete pyrolytic process.
As shown in Fig. 1 to 5, the structure of pyrolysis oven of the present invention is as follows:
This pyrolysis oven is comprised of pyrolysis unit stove 11, and each pyrolysis unit stove 11 structure is identical, and pyrolysis unit stove arrangement mode is double placement arranged side by side.Pyrolysis unit stove is with thermal insulation layer outward, and thermal insulation layer 10 is followed successively by fire brick layer 101, asbestos layer 102, undercloak 103 (as shown in Figure 1, internal structure is as shown in Fig. 3,4,5 for profile) from inside to outside.
Fire brick layer 101 adopts pattern structure while building by laying bricks or stones with pyrolysis unit stove, and fire brick layer 101 seals with refractory materials with pyrolysis unit stove junction, guarantees that destructive distillation chamber and combustion chamber and outside atmosphere are isolated.Between fire brick layer and peripheral undercloak, have the cavity that 100mm is thick, fill asbestos in cavity, asbestos play insulation effect (as shown in Fig. 3,4,5) to body of heater.
Each pyrolysis unit stove 11 is comprised of feeding unit 9, destructive distillation chamber 6, combustion chamber 7 and solid materials cooling discharge device ().Feeding unit 9 is placed in body of heater top, trapezoidal hopper storage bin and rotary pocket feeder, consists of, and feed opening matches and is connected (as shown in Figure 1, 2) with destructive distillation chamber upper dimension.
Destructive distillation chamber is all comprised of high temperature resistant unit cylindrical shell, destructive distillation chamber is high temperature resistant, and unit cylindrical shell Outside Dimensions is 1500mm * 400mm * 500mm, wall thickness 40mm, destructive distillation chamber unit cylindrical shell top is added with inlays draw-in groove (as Fig. 6), draw-in groove wall thickness 40mm, draw-in groove sub-buckle edge casts with cylindrical shell is integrated, draw-in groove degree of depth 40mm, and sub-buckle is along height 60mm; Inner barrel has a swash plate that slides and move down for solid materials along inner side-wall 1500mm length direction, edge and angled connection of the long sidewall of cylindrical shell on swash plate, under swash plate, along along continuous straight runs under another the long sidewall of cylindrical shell with destructive distillation chamber, there is 60mm interval, the swash plate back side is uniformly distributed 2 gussets with pyrolysis furnace superintendent sidewall and is connected with long sidewall with the swash plate back side, and object is to increase swash plate holding capacity and improve heat transfer efficiency; On the short side of cylindrical shell of destructive distillation chamber, the drift angle place, Delta Region that swash plate and sidewall form has diameter 40mm, circular hole of the same size, and this circular hole works to derive gas; At circular hole outer wall, have a pipe connecting (being the take-off pipe of carbonization gas collection tube 4), pipe connecting one end is connected with circular hole, and one end is connected with the vertical collecting pipe of body of heater, and object is that the supervisor of the gas derivation introducing carbonization gas collection tube 4 of each air chamber is gathered.Build along short transverse destructive distillation chamber.Under each is high temperature resistant cylindrical shell along being connected along draw-in groove with in another cylindrical shell sub-buckle, inner swash plate opposite direction, cylindrical shell interlocks assembled up and down successively, builds certain altitude by laying bricks or stones and meets manufacturing technique requirent (as shown in Figure 2).
Combustion chamber consists of each combustion chamber unit, each combustion chamber unit structure is: a gas conduct pipe (being minute segmental bronchus of gaspipe 5) one end is connected with Verticle gas supply pipe 5, one end is connected with lighting-up tuyere, combustion chamber internal point burner is upper and lower forms high-temperature flue gas operation passage along dividing plate and Inner Wall of Combustion Chamber are all set, on lighting-up tuyere, along dividing plate near-end, be close to lighting-up tuyere sidewall, upper along dividing plate far-end and far-end sidewall maintenance 200mm distance, under lighting-up tuyere, along dividing plate and lighting-up tuyere proximal, side wall, keep 200mm distance, along dividing plate far-end and far-end sidewall, be close to down, the high-temperature flue gas of lighting-up tuyere burning in combustion chamber unit inside along the passage rising of turning back, the height of combustion chamber unit is the height of 2 destructive distillation chamber cylindrical shells.Combustion chamber unit is built along short transverse, and the smoke evacuation that high-temperature flue gas forms at internal partition, with turning back under rising passway effect, is progressively risen with S shape, with body of heater top smoke-uptake, discharges (as shown in Figure 4,5).
Bottom, destructive distillation chamber is connected with solid materials cooling discharge device, cooling discharge device is become with round metal tubular heat exchanger set by spiral discharging device, spiral discharging device closes and is connected with destructive distillation chamber lower seal, discharger end discharge port forms certain angle (315 °) airtight connection with cylindrical heat exchanger, cylindrical heat exchanger discharging port is downward-sloping, and material can freely be discharged under action of gravity.Except spiral discharging device top motor and metallic cylinder interchanger discharge port, other solid materials cooling discharge devices are all placed in water coolant, realize material dry method temperature-fall period.
Beneficial effect of the present invention is as follows:
(1) adaptability to raw material is strong: all solids that are less than 30mm are without bonding pulverulent material, all can in this pyrolysis oven, realize pyrolytic process, overcome the technical bottleneck that existing vertical heater cannot pyrolysis small particle size solid material, its raw material is applied widely, and the non-caked material of solid all can be used.
(2) thermo-efficiency is high: this pyrolysis oven between adjacent destructive distillation chamber, arrange one combustion chamber shared, destructive distillation chamber adopts high temperature heat-resistant to conduct fast material, combustion chamber high temperature flue gas and destructive distillation chamber outer wall direct contact heat transfer, the indoor material of destructive distillation can directly contact with high temperature resistant material heating surface in folding process, realize Rapid Thermal conduction, thermo-efficiency is high; And by the indoor blanking swash plate being crisscross arranged of destructive distillation, solve the inhomogeneous problem of heating raw materials; And can solve by the combustion chamber of special construction the problem that the dust in small particle size raw material pyrolytic process produces and controls; Employing external-heat heating, improves pyrolysis gas purity and has reduced the load of follow-up purification system.
(3) equipment life is long, stable: body of heater is inner adopts high temperature resistant, wear-resistant, resistance to oxidation, special materials manufacture that ultimate compression strength is high, service life of equipment is long, maintenance cycle is long, the attached relevant equipment of body of heater is simple, and level of automation is high, can realize production run steady in a long-term; And adopt the cooling dry coke quenching of closed water cycle, can water saving effective semicoke quality of controlling.
(4) product quality is high, oil gas product yield is large: this pyrolysis oven adopts the destructive distillation of external-heat segmentation method of temperature control, each pyrolysis unit is outdoor pyrolysis and combustion chamber, arbitrarily regulating gas amount and air quantity, reach the interior temperature-stable of pyrolysis oven controlled, the oil gas dustiness that pyrolysis produces is little, and gas production rate is large, and gas heating value is high, solid materials steady quality, all products are the deep processing of suitable downstream all.
(5) pyrolytic process less energy-consumption: while utilizing this pyrolysis oven to carry out pyrolysis, whole pyrolytic process process takes full advantage of material gravity, primary structure all utilizes action of gravity design, and material water consumption current consumption in pyrolytic process is few.
The above; be only the present invention's embodiment preferably, but protection scope of the present invention is not limited to this, is anyly familiar with in technical scope that those skilled in the art disclose in the present invention; the variation that can expect easily or replacement, within all should being encompassed in protection scope of the present invention.Therefore, protection scope of the present invention should be as the criterion with the protection domain of claims.
Claims (10)
1. an outer hot vertical tilting pyrolysis oven, is characterized in that, comprising:
Body of heater, is vertically provided with some destructive distillation chamber and some combustion chambers in it, described destructive distillation chamber and interval, described combustion chamber arrange, and described destructive distillation chamber is not communicated with mutually with described combustion chamber; The indoor fuel decline passway that is equipped with vertical setback shape of described each destructive distillation;
Feeding unit, is arranged on described body of heater upper end, is communicated with the upper end open of some destructive distillation chamber in described body of heater;
Carbonization gas collection tube, is arranged on described body of heater, is communicated with respectively with the some destructive distillation chamber in described body of heater;
Gaspipe, is arranged on described body of heater, is communicated with respectively with the some combustion chambers in described body of heater;
Cooling tank, is arranged on described bottom of furnace body;
Spiral discharging device, is arranged in described cooling tank, is communicated with the lower ending opening of destructive distillation chamber in described body of heater.
2. outer hot vertical tilting pyrolysis oven according to claim 1, is characterized in that, the indoor fuel decline passway that is equipped with vertical setback shape of described each destructive distillation is formed by following structure:
Some swash plates, are stratified and set on indoor two the relative inwalls of described destructive distillation from top to bottom;
The strut member that supports use is all set between described each swash plate and this swash plate place inwall;
In described some swash plates, the swash plate upper end in odd-level is fixed on the indoor side inwall of described destructive distillation, and the swash plate in even level is fixed on the opposite inwall of a described side inwall;
Each swash plate lower end is to the free end of the indoor oblique below inclination of described destructive distillation, keeps interval with described opposite inwall, and keeps interval with the swash plate of this swash plate below;
The lower end of two neighbouring swash plates refers in the opposite direction;
The plate face of indoor each swash plate from top to bottom of described destructive distillation and each swash plate lower end are communicated with into the fuel decline passway of vertical setback shape far from interval and each swash plate lower end of opposite inwall far from the interval of below swash plate.
3. outer hot vertical tilting pyrolysis oven according to claim 1, is characterized in that, described body of heater by the identical some pyrolysis unit stoves of structure from top to bottom layering setting be formed by connecting;
Wherein, be equipped with some destructive distillation chamber and some combustion chambers in each pyrolysis unit stove, described destructive distillation chamber and interval, described combustion chamber arrange, and described destructive distillation chamber is not communicated with mutually with described combustion chamber;
In described each pyrolysis unit stove, be equipped with swash plate and be supported on this swash plate and its place inwall between strut member, each swash plate lower end is the free end that tilts to the indoor oblique below of described destructive distillation, keeps interval with opposite inwall;
Swash plate in neighbouring two pyrolysis unit stoves arranges towards the opposite;
After described some pyrolysis unit stove connects, form several whole destructive distillation chambers and several whole combustion chambers, the plate face of the swash plate in indoor each pyrolysis unit stove from top to bottom of described each whole destructive distillation and each swash plate lower end are communicated with into the fuel decline passway of vertical setback shape far from interval and each swash plate lower end of opposite inwall far from the interval of below swash plate.
4. according to the outer hot vertical tilting pyrolysis oven described in claim 1,2 or 3, it is characterized in that, also comprise: partition wall is horizontally installed in described body of heater, be connected between the antetheca and rear wall in described body of heater, the some destructive distillation chamber in described body of heater and some combustion chambers are divided into two portions.
5. according to the outer hot vertical tilting pyrolysis oven described in claim 1,2 or 3, it is characterized in that, described carbonization gas collection tube is two groups, divides the both sides that are located at described body of heater;
Described every group of carbonization gas collection tube forms with some take-off pipes that interval is connected on described supervisor from top to bottom by supervisor, and each take-off pipe is connected to the bending part of the fuel decline passway of the indoor vertical setback shape of described destructive distillation.
6. according to the outer hot vertical tilting pyrolysis oven described in claim 1,2 or 3, it is characterized in that, described gaspipe is two groups, divides the both sides that are located at described body of heater;
Described every group of gaspipe by main tracheae and some minutes segmental bronchuses that interval is connected on described main tracheae from top to bottom form, each branch's tracheae is communicated with respectively with in described combustion chamber.
7. according to the outer hot vertical tilting pyrolysis oven described in claim 1,2 or 3, it is characterized in that, described body of heater is rectangular structure, and the outer wall of body of heater is thermal insulation layer.
8. outer hot vertical tilting pyrolysis oven according to claim 7, is characterized in that, described thermal insulation layer is three-decker, and wherein, skin is fire brick layer, and middle layer is asbestos layer, and internal layer is undercloak.
9. outer hot vertical tilting pyrolysis oven according to claim 8, it is characterized in that, described feeding unit consists of trapezoidal hopper storage bin and the rotary pocket feeder that is arranged on described trapezoidal hopper storage bin bottom, and the feed opening of described rotary pocket feeder is communicated with the upper end open coupling of the destructive distillation chamber of described body of heater.
10. according to the outer hot vertical tilting pyrolysis oven described in claim 1,2 or 3, it is characterized in that, inside, described combustion chamber is provided with several lighting-up tuyeres, and the upper and lower edge of described each lighting-up tuyere all arranges dividing plate, and each dividing plate and described Inner Wall of Combustion Chamber form the rising passway of turning back that high-temperature flue gas is discharged; Wherein, the near-end along dividing plate on described each lighting-up tuyere is adjacent to this lighting-up tuyere place sidewall, described upper along dividing plate far-end and far-end sidewall maintenance 200mm distance; Under described each lighting-up tuyere, along dividing plate and this lighting-up tuyere place proximal, side wall, keep 200mm distance, described be adjacent to along dividing plate far-end and far-end sidewall down; Each dividing plate forms the rising passway of turning back of smoke evacuation in described combustion chamber.
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Cited By (5)
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|---|---|---|---|---|
| CN107227161A (en) * | 2016-08-25 | 2017-10-03 | 王刚 | Be carbonized less boiler |
| CN107236552A (en) * | 2017-03-26 | 2017-10-10 | 王刚 | Be carbonized less boiler |
| CN109554182A (en) * | 2018-11-27 | 2019-04-02 | 王守信 | The carbide furnace of gas collection fistulae and Flapper type |
| CN111057558A (en) * | 2019-12-31 | 2020-04-24 | 山东钢铁集团日照有限公司 | Application method of hydrogen-rich gas generated after LNG (liquefied Natural gas) process in coke oven heating |
| CN111793506A (en) * | 2020-07-20 | 2020-10-20 | 程建坤 | Energy-saving emission-reducing coal tar extractor with cleaning function |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101343544A (en) * | 2008-09-03 | 2009-01-14 | 吴启成 | Vibrating turning mixed flow type complete-alternation granule wax shale destructive distillation method and device |
| CN201729799U (en) * | 2010-08-19 | 2011-02-02 | 西峡龙成特种材料有限公司 | Vertical coal decomposition device with horizontal insertion gas pipe |
| CN102102022A (en) * | 2010-12-31 | 2011-06-22 | 清华大学 | Moving bed reactor for medium temperature dry distillation |
| CN102199437A (en) * | 2011-04-23 | 2011-09-28 | 华北电力大学（保定） | Large-scale low-order brown coal upgrading tower |
| CN202214324U (en) * | 2011-06-30 | 2012-05-09 | 宜宾天原集团股份有限公司 | Heat adjustable formed coke carbonization furnace |
| CN202415455U (en) * | 2011-12-31 | 2012-09-05 | 辽宁志远筛子王制造有限公司 | Small-particle oil shale retort with elastic rod vibrating body |
| CN103160291A (en) * | 2011-12-09 | 2013-06-19 | 新疆美特镁业有限公司 | Powdered coal coking device and powdered coal coking method |
| CN203319929U (en) * | 2013-05-31 | 2013-12-04 | 李秋生 | Carbon substance vibrating pyrolysis tower |
-
2014
- 2014-05-07 CN CN201410190452.0A patent/CN103937521B/en not_active Expired - Fee Related
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101343544A (en) * | 2008-09-03 | 2009-01-14 | 吴启成 | Vibrating turning mixed flow type complete-alternation granule wax shale destructive distillation method and device |
| CN201729799U (en) * | 2010-08-19 | 2011-02-02 | 西峡龙成特种材料有限公司 | Vertical coal decomposition device with horizontal insertion gas pipe |
| CN102102022A (en) * | 2010-12-31 | 2011-06-22 | 清华大学 | Moving bed reactor for medium temperature dry distillation |
| CN102199437A (en) * | 2011-04-23 | 2011-09-28 | 华北电力大学（保定） | Large-scale low-order brown coal upgrading tower |
| CN202214324U (en) * | 2011-06-30 | 2012-05-09 | 宜宾天原集团股份有限公司 | Heat adjustable formed coke carbonization furnace |
| CN103160291A (en) * | 2011-12-09 | 2013-06-19 | 新疆美特镁业有限公司 | Powdered coal coking device and powdered coal coking method |
| CN202415455U (en) * | 2011-12-31 | 2012-09-05 | 辽宁志远筛子王制造有限公司 | Small-particle oil shale retort with elastic rod vibrating body |
| CN203319929U (en) * | 2013-05-31 | 2013-12-04 | 李秋生 | Carbon substance vibrating pyrolysis tower |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107227161A (en) * | 2016-08-25 | 2017-10-03 | 王刚 | Be carbonized less boiler |
| CN107236552A (en) * | 2017-03-26 | 2017-10-10 | 王刚 | Be carbonized less boiler |
| CN109554182A (en) * | 2018-11-27 | 2019-04-02 | 王守信 | The carbide furnace of gas collection fistulae and Flapper type |
| CN111057558A (en) * | 2019-12-31 | 2020-04-24 | 山东钢铁集团日照有限公司 | Application method of hydrogen-rich gas generated after LNG (liquefied Natural gas) process in coke oven heating |
| CN111793506A (en) * | 2020-07-20 | 2020-10-20 | 程建坤 | Energy-saving emission-reducing coal tar extractor with cleaning function |
| CN111793506B (en) * | 2020-07-20 | 2021-10-12 | 程建坤 | Energy-saving emission-reducing coal tar extractor with cleaning function |
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