CN203794835U - HY type dry distillation furnace - Google Patents
HY type dry distillation furnace Download PDFInfo
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- CN203794835U CN203794835U CN201420185555.3U CN201420185555U CN203794835U CN 203794835 U CN203794835 U CN 203794835U CN 201420185555 U CN201420185555 U CN 201420185555U CN 203794835 U CN203794835 U CN 203794835U
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Abstract
An HY type dry distillation furnace is characterized in that the dry distillation furnace is composed of multiple dry distillation subunits and each dry distillation subunit is composed of a feeding device, an oil-gas discharging device, a dry distillation device, a heating device and a coke extraction device; dry distillation is conducted on materials through the furnace in the mode that radiant heat exchange and heat convection are combined; gas generated in the dry distillation process is used as a dry distillation heat source and self-balance of dry distillation heat can be achieved; the materials are directly heated through radiation of the furnace wall of a combustion chamber and a heat carrier does not need to be secondarily heated and transported in a long distance; a dry distillation gas guiding device is arranged in the furnace and gas inside the furnace flows smoothly; coke is extracted in a dry method. The dry distillation furnace is high in heat use efficiency, the gas amount of an outlet is small, water consumption is small, and the oil recovery rate is high. The daily capacity of the dry distillation furnace is large and can reach over 6000 tons and the dry distillation furnace is suitable for medium-temperature and low-temperature dry distillation oil refinement of the materials such as oil sand, oil shale and coal and suitable for dry distillation oil refinement of large particle materials and small particle materials with the diameter smaller than 15mm.
Description
Technical field
The present invention relates to a kind of gas retort that adds thermal material, carbonizing gas layering is derived, taked dry method to discharge of the coke with radiation mode.Be applicable to various particle diameters, comprise the middle low-temperature pyrolysis oil refining of the materials such as short grained resinous shale, oil-sand and coal.
Background technology
At present, domestic in material, low-temperature pyrolysis stove all can not process small particles material, causes a large amount of wastes of resource.Resinous shale out of general mining, coal, oil-sand etc., what be less than 12mm particle diameter accounts for 20%～30%, and high reaches 40%～50%.In, low-temperature pyrolysis stove application more have three kinds.The first is Fushun type retort, for columnar structured, is internal combustion type stove, uses recuperative heater to coordinate, and heat exchange mode is convective heat exchange.During work, with gas blower, from gas retort bottom, send into saturated air combustion-supporting, the flue gas that fixed carbon burning in material produces carries out destructive distillation to the resinous shale on top, for preventing the coking of inner flue gas of the stove excess Temperature, on gas retort top, pass into and through regenerative heater, be heated to the gas of 550 ℃～650 ℃ and regulate.Fushun type retort can not be processed small particles material, and gas retort material handling granularity is generally 12～75mm, can only process the material of the above particle diameter of 20mm when material moisture is high, and single stove processing power is 100 tons.The second is Huadian formula full circulation carbonization furnace, for circle square structure, top is circular, bottom is square, stove is interior without combustion unit, dependence is heated to the thermal circulation gas of 650 ℃ of left and right resinous shale is carried out to destructive distillation through regenerative heater, this stove heat exchange mode is convective heat exchange, can not process small particles material.General processing granularity is 6～50mm, can only process the material of the above particle diameter of 20mm when material moisture is high, and single stove processing power is 300 ton per days.The third is Maoming formula gas retort, is square structure, is internal combustion type stove, is commonly called as Gas stove, is not equipped with process furnace.During work, from gas retort bottom, pass into flammable gas and air, the flue gas that burning produces carries out destructive distillation to the material on top in uphill process, and this stove heat exchange mode is convective heat exchange, can not process small particles material, general processing granularity is 30～120mm, and single stove processing power is 200 ton per days.This gas retort produces the high-temperature flue gas of 1000 ℃ of left and right while burning in stove due to gas, usually cause slagging to be forced to blowing out cleaning, and inevitably burnt again a part of oil gas during burning, oil recovery rate is lower, exit gas is sneaked into because of flue gas, and calorific value is lower.Formula side, Maoming stove starts for oil shale retort oil refining, because the problems referred to above and pollution problem all stop production the eighties in 20th century.After having some areas that this stove is transformed after 21 century, for coal carbonization, produce blue carbon.But these defects still exist.Fushun formula, Huadian formula gas retort heat exchange mode are all convective heat exchanges, but need to build separately process furnace, then thermal barrier are transported to gas retort by pipeline.Although convection heat transfer intensity is large, but defect is that the permeability of material in stove is required to height, and thermal barrier needs second-heating, and in course of conveying, thermal losses is larger, thermo-efficiency is low, have by destructive distillation material because self air content is low, after second-heating, system thermal can not balance, be forced to from external complement heat, cause system process complicated, investment strengthens, and operation is loaded down with trivial details.Maoming formula gas retort is to rely on convective heat exchange to add thermal material equally, although do not need to build separately process furnace, due to temperature of combustion in gas retort far beyond in, the temperature that needs of low-temperature pyrolysis, easily cause the disadvantages such as slagging, oil firing gas.The type of furnace of these several gas retorts all has treatment capacity little, and floor space is large, can not process the defects such as small particles material, and use is restricted, and can not meet the needs of large-scale industrial production.For this reason, a kind of novel safety performance gas retort high, that thermo-efficiency is high, that can process small particles material, that can maximize is badly in need of in China.
Summary of the invention
The object of the present invention is to provide a kind of safety performance high, can process small particles material, power consumption is few, thermo-efficiency is high, technique is simple, the gas retort that processing power is large.For realizing the object of this invention, need the key technical problem solving to be:
1, solve the problem that in stove, material makes destructive distillation not carry out because permeability is bad.Designing a kind of material and in stove, flow smooth and easyly, be subject to thermal balance,, there is not the phenomenons such as obstruction, scaffold, is suitable for the gas retort of small particles material destructive distillation in the smooth and easy discharge of carbonization gas physical efficiency in stove.
2, the expansion of solution gas retort capacity is subject to the uniform distribution of material in gas retort, the restricted problem of even exhaust.After designing a kind of gas retort capacity and expanding, still can thermally equivalent by destructive distillation material, the gas retort of balanced destructive distillation, the smooth and easy discharge of carbonization gas physical efficiency.
3, solving thermal barrier needs second-heating to cause thermosteresis, the problem that gas retort heating efficiency is not high.From the structure design of gas retort, start with, improve the utilising efficiency of destructive distillation heat, simplify heating system, shorten flow process, reduce system thermal loss.
4, solve the problem that gas retort outlet is large-minded, calorific value is low, oil recovery system is huge.From the structure design of gas retort, start with, make outlet of still tolerance minimum, reduce sneaking into of non-carbonizing gas, improve the calorific value of carbonization gas, thus the plant capacity of reduction oil recovery system, power consumption and the running cost of minimizing system.
5, solve the problem of gas retort to the selective restriction of destructive distillation material.Design a kind of to the adaptable gas retort of material, not only can carry out destructive distillation to the large material of particle diameter, also can carry out destructive distillation to the little material of particle diameter, can meet multiple user's demand and the material of multiple quality carries out destructive distillation, not only can be used for oil shale retort, and can be used for oil-sand and coal carbonization.
6, solve the problem of gas retort long period safety, steady running.In gas retort structure design, improve its security, there is no serious potential safety hazard, there is no gas leakage, there is no sewage discharge, prevent obstruction, coking in stove, the generation of the security incidents such as prevent exploding.
HY type gas retort of the present invention can solve the problems of the technologies described above preferably, realizes goal of the invention.Its technology characteristics is: take mode that convective heat exchange and radiation heat transfer combine to material destructive distillation; Utilization is directly burnt gas that material produces in retort process as destructive distillation thermal source in combustion chamber, do not need thermal barrier to carry out second-heating and remote conveying; Utilize the furnace wall of combustion chamber as thermophore, by the mode of radiation heat transfer, material is carried out to direct heating; With furnace wall, by the isolation of combustion chamber and destructive distillation chamber, prevent that flue gas from sneaking into carbonizing gas, reduce outlet of still tolerance; Carbonizing gas layering take-up gear is set in gas retort, guarantees the permeability of furnace gas; Use heat storage technology warm-up combustion-supporting air, reduce funnel temperature, improve thermo-efficiency; Utilize cold gas by the mode of convective heat exchange, to reclaim the waste heat of semicoke, reduce coke discharging temperature, improve thermo-efficiency; Utilize carbonizing gas to carry out preheating and drying material by the mode of convective heat exchange, and reduce the temperature of carbonizing gas outlet, make the gas temperature that enters oil recovery system lower than 120 ℃; By dry method, discharge of the coke and replace wet method to discharge of the coke, reduce the consumption of water.
Technical process of the present invention is:
1, by the technical process of destructive distillation material: material adds from gas retort top, enter preheating and drying chamber, the carbonizing gas of the approximately 500-550 ℃ left and right that material is derived in gas retort is heated to 200 ℃～250 ℃, the moisture that material contains all evaporates, material continues to come downwards to the destructive distillation chamber that both sides are combustion chamber furnace wall, material absorbs the radiations heat energy of both sides furnace wall in destructive distillation chamber, and temperature rises to 500 ℃～550 ℃, realizes complete destructive distillation.Semicoke after destructive distillation continues descending, enter cooling room, material is in cooling room, and the cold gas of 35 ℃-40 ℃ being sprayed by both sides is cooled to 150 ℃～200 ℃, through cold burnt case, be cooled to 120 ℃ of following discharges again, the rotary conveyor that is finally arranged at cold burnt lower box part is transported to stockyard.
2, the technical process of destructive distillation gas: gas retort both sides and middle part are equipped with independently gas take-up gear, the carbonizing gas producing in retort process and the cold gas passing into from gas retort bottom cooling room are imported into the gas chamber that is arranged at top, combustion chamber, carbonizing gas sprays from gas chamber, enter preheating and drying chamber, carbonizing gas carries out after preheating and drying material, temperature is reduced to below 120 ℃, through being arranged at air chamber and the carbonizing gas collecting tubule at gas retort top, discharge, through reclaiming the oily substance wherein containing, be cooled to 35 ℃～40 ℃ after separated moisture, a part is sent into combustion chamber by gas blower fan and is used as fuel, a part enters gas retort bottom for cooling semicoke, redundance is sent into gas holder storage and is separately used it for anything else.
3, the technical process of flue gas: air enters regenerator and is preheating to more than 500 ℃, with fuel gas in combustion chamber mixed firing, the high-temperature flue gas that burning produces is 900 ℃～1000 ℃, both sides furnace wall is heated to more than 700 ℃, high-temperature flue gas enters regenerator, by thermal exchange, to heat storage, flue-gas temperature is lowered to 150 ℃ of following rear discharges.This installs each destructive distillation unit and is provided with two regenerator, two combustion chambers, alternate cycles is used, with the temperature all-the-time stable that guarantees both sides, combustion chamber furnace wall more than 700 ℃.Furnace wall gives heat radiation by destructive distillation material, by heating material to 500 ℃～550 ℃, makes material generation destructive distillation.
By the technical process three of the technical process of the technical process of destructive distillation material, destructive distillation gas, flue gas, mutually combined and formed the flow process of HY type distillation process, and form complete, continuous distillation process.
HY type gas retort of the present invention, its constitutional features is: gas retort is comprised of a plurality of destructive distillation subelements, each destructive distillation subelement is comprised of feeding device, oil gas discharger, destructive distillation device, heating unit, discharging device for coke.Figure 1 shows that a HY type gas retort structural representation that has 1 destructive distillation subelement.
The constitutional features of described feeding device is: feeding device is arranged at the top of gas retort, by feed bin, hopper, two slide valves, formed, wherein first slide valve is arranged between feed bin and hopper, second slide valve is arranged at hopper bottom, and hopper communicates through the preheating and drying chamber of second slide valve and destructive distillation device;
The constitutional features of described oil gas discharger is: oil gas discharger is arranged at the top of destructive distillation device, air chamber and carbonizing gas collecting tubule, consists of; The preheating and drying chamber of air chamber bottom and destructive distillation device communicates, and top is connected with carbonizing gas collecting tubule;
The constitutional features of described destructive distillation device is: destructive distillation device is comprised of preheating and drying chamber, destructive distillation chamber, cooling room, carbonizing gas guidance device; Preheating and drying chamber, destructive distillation chamber, cooling room are arranged in order from top to bottom; The furnace wall that both sides, destructive distillation chamber are combustion chamber; Carbonizing gas guidance device is comprised of carbonizing gas guiding channel and gas chamber; Carbonizing gas guiding channel is arranged in the furnace wall of combustion chamber, and gas chamber is arranged at the top of combustion chamber, and carbonizing gas guiding channel and gas chamber communicate, and gas chamber is provided with carbonizing gas ejiction opening; Cooling room is arranged at the bottom of destructive distillation chamber, and cooling room both sides are provided with cold gas and enter pipe and cold gas spout, and cooling room bottom and cold burnt case communicate;
The constitutional features of described heating unit is: heating unit enters pipe, gas burner, preheated air by combustion chamber, regenerator, fuel gas and enters pipe, and smoke discharge tube, reversing valve, combustion air gas blower, smoke evacuation induced draft fan, fuel gas blower fan form; The heating unit of a unit is provided with two combustion chambers, two regenerator; Combustion chamber is arranged at the both sides of destructive distillation chamber, and gas burner is arranged in combustion chamber, and gas burner enters pipe with fuel gas, fuel gas blower fan is connected successively; Regenerator is arranged at combustion chamber lower outside, and heat storage is housed in regenerator, and regenerator is provided with preheated air and enters pipe, and smoke discharge tube is connected with combustion air gas blower, smoke evacuation induced draft fan respectively; Fuel gas enters pipe and preheated air and enters reversing valve is installed on pipe;
The constitutional features of described discharging device for coke is: discharging device for coke is arranged at gas retort bottom, the burnt plate of cold burnt case, coke extractor, gear, cold gas access tube, steam access tube, water coolant access tube, two slide valves and rotary conveyor, consists of; Coke extractor, keep off burnt plate and be arranged in cold burnt case, cold burnt casing is provided with cold gas access tube, steam access tube, water coolant access tube, and cold burnt lower box part is provided with two slide valves and rotary conveyor.
The principle of work of the heating unit of HY type gas retort of the present invention is shown in Fig. 2.Each destructive distillation unit is equipped with two combustion chambers, two regenerator, by the switching of air and gas reversing valve, alternate cycles is used, with the temperature all-the-time stable that guarantees both sides, combustion chamber furnace wall more than 700 ℃.First flow process of heating unit work is: fuel gas is in the I Indoor Combustion of burning, the high-temperature flue gas producing is heated to furnace wall more than 700 ℃, furnace wall by radiation by heat pass in destructive distillation chamber by destructive distillation material, flue gas enters II regenerator waste heat is exchanged to heat storage, is reduced to 150 ℃ and discharges out of the furnace; After the heat that combustion air is accumulated at I regenerator absorption heat storage, mix with fuel gas, support burning; Second flow process of heating unit work is: after the switching of reversing valve, fuel gas is in the II Indoor Combustion of burning, and combustion air absorbs heat in II regenerator.So go round and begin again, move in circles, form continuous heating process.
HY type gas retort of the present invention, its constitutional features is: gas retort is comprised of a plurality of destructive distillation subelements; The preheating and drying section on the gas retort top that a plurality of destructive distillation subelements form is interconnected.The gas retort structural representation that Fig. 3 is comprised of 3 destructive distillation subelements.
The quantity of the destructive distillation subelement of HY type gas retort of the present invention treatment capacity is as required selected.When the treatment capacity that needs is large, destructive distillation subelement can be established some more, needs gas retort treatment capacity hour, and destructive distillation subelement can be established less.Generally, the day output of 1 destructive distillation subelement is 50～100 tons.Such as, as wanted, make the day output of gas retort reach 2000 tons of left and right, need to arrange 20～40 destructive distillation subelements.
HY type gas retort of the present invention is compared with Fushun, Maoming, Huadian formula gas retort, has following features:
1, HY type gas retort of the present invention can be processed small particles material.Material total height in Fushun, Maoming, Huadian formula gas retort is generally 10m left and right, when adopting gaseous heat-carrier distillation process, because small particles material space is little, air-flow is difficult to pass through, and resistance is very large, general gas flow needs the pressure head of 1500Pa-2000Pa while passing through the small-particle bed of material of 1m height.Therefore when using Fushun, Maoming, Huadian formula gas retort to process small particles material, need the pressure head of 20000Pa left and right can penetrate the bed of material, and airing system generally can not provide high like this gas head, even if high like this pressure head is provided, in stove, material is in fluidized state, outside a large amount of little material effusion stoves, so pressure head is little, in stove, often there is the phenomenons such as obstruction, scaffold, pressure head is large, there is again latch up phenomenon outward in stove, gaseous heat-carrier is difficult to and material uniform contact, and destructive distillation is difficult to carry out continuously.This technique retort section relies on the radiation heat transfer of both sides furnace wall to material, no longer rely on convective heat exchange, furnace pressure is lower, and be provided with the guidance device of carbonizing gas, carbonizing gas does not pass through the whole bed of material, and the maximum height of passing through the bed of material is 3m left and right, and the pressure head needing is 5000Pa-6000Pa, this pressure head is easy to realize in process system, so retort section there will not be the phenomenons such as obstruction, scaffold.Therefore making to process small particles material becomes possibility.
2, HY type gas retort heat utilization rate of the present invention is high, and thermo-efficiency is high, energy-conservation.The present invention has adopted multiple conservation measures, utilizes the gas of destructive distillation generation as fuel, has realized system heat energy self-equilibrating, without outer concurrent heating source; Utilize heat storage technology warm-up combustion-supporting air, funnel temperature is dropped to below 150 ℃; Heating and material destructive distillation are integrated, have cancelled process furnace in traditional technology and the transport pipe of high-temperature heat carrier, to material direct heating, reduced heat-energy secondary conversion, conveyance loss and heat lost by radiation; Utilize cold gas by convective heat exchange, to reclaim the waste heat of semicoke, heat transfer intensity is large, and the heat of recovery is directly used in the destructive distillation of material.These measures have all improved the utilization ratio of heat energy greatly, and energy-saving effect is obvious.Particularly for the low material of air content, realize retort process heat self-balancing significant.The gas heat carrier of Fushun, Huadian distillation process is at stove external heat, and charging temperature is controlled at 650 ℃ of left and right, and the heat-energy secondary conversion in heat-processed, the heat lost by radiation of process furnace, the thermosteresis in thermal barrier course of conveying are all very large.
3, HY type gas retort outlet of the present invention is narrow-minded, is conducive to simplify oil recovery system.HY type gas retort of the present invention has adopted the technology of radiation formula direct heating material, and furnace wall is separated heating and destructive distillation, in the gas that destructive distillation produces, does not sneak into flue gas and gaseous heat-carrier.Therefore gas retort outlet tolerance only has the 30-50% left and right of Fushun, Maoming, Huadian formula gas retort.This has just alleviated the pressure of oil recovery system greatly.In retort process, flue gas be heated material and directly do not contact, greatly reduce gas retort outlet tolerance, thereby also greatly reduce the load of oil recovery system.The thermal barrier of Fushun, Maoming distillation process is the mixture of destructive distillation gas and flue gas, and the thermal barrier of Huadian distillation process is destructive distillation gas, thermal barrier all with by destructive distillation material, directly contacted.These three kinds of techniques have a large amount of gaseous heat-carriers to enter gas retort, and the gas finally producing with destructive distillation discharges out of the furnace, thereby gas retort outlet tolerance is very large, cause rear portion oil recovery system load to increase.
4, HY type gas retort treatment capacity of the present invention is large, is suitable for large-scale industrial production.HY type gas retort of the present invention has been taked the method for unit combination, each destructive distillation subelement is all relatively independent destructive distillation main bodys, can complete separately the destructive distillation task to material, when several destructive distillation subelements are combined, just can increase substantially the treatment capacity of gas retort.Day output maximum can reach more than 6000 tons, and maximum ATP gas retort is suitable in the world.Fushun, Maoming, Huadian formula gas retort, owing to can not solving the equiblibrium mass distribution of furnace gas, material, cannot expand capacity, and maximum day output can only reach 500 tons.The maximization of gas retort list stove treatment capacity, this extensive, industrialization to the pyrogenation and carbonization Efficient Conversion industry of resinous shale, the industry of oil-sand destructive distillation oil refining, coal, the facility investment, the operational management cost that reduce unit ore deposit amount are significant.
5, HY type gas retort water saving of the present invention.HY type gas retort bottom adopts dry method to discharge of the coke, and semicoke water content can be controlled at below 6%, and Fushun, Maoming, Huadian formula gas retort all adopt wet method to discharge of the coke, and general semicoke water content is in 20% left and right.The scale of construction of working off one's feeling vent one's spleen due to HY type gas retort is only the 30-50% left and right of Fushun, Maoming, Huadian formula gas retort in addition, so the refrigeration cycle water consumption of rear portion oil recovery system also will be than Fushun, Maoming, the low 50-70% of Huadian formula gas retort left and right.
6, HY type gas retort strong adaptability of the present invention, be applicable to various materials, comprise the materials such as oil-sand, resinous shale and coal in, low-temperature pyrolysis oil refining, because its main heat exchange mode is radiation heat transfer, therefore to material oil length height, water content number, air content number there is no obvious exclusiveness, the scope of application is more wide in range.Both be applicable to in large granular materials, low-temperature pyrolysis oil refining.Also be applicable to be less than 15mm material in, low-temperature pyrolysis oil refining.
7, HY type gas retort safety in operation of the present invention, reliability are high.The gas retort of traditional technology be in operation gas and coal-char combustion, there is air to enter, have combustion processes, all have coking, obstruction, the possibility of blast even occur, Fushun formula distillation process, Maoming formula distillation process, because all containing oxygen in carbonizing gas, all have the record of blasting.And in HY type gas retort of the present invention because separate combustion chamber and destructive distillation chamber, the gas that flue gas and destructive distillation produce does not cross, and the high-temperature flue gas producing during burning, even if there is air remaining, because it does not directly contact with destructive distillation gas, the possibility of also just not blasting.Destructive distillation is indoor without combustion unit, does not have oxygen to enter, and can not produce the problems such as local superheating, coking, obstruction, and gas retort starting and blowing out are all simple and convenient, opens the igniting of gas valve and can start, and closed gas valve gets final product blowing out; Movement-less part in gas retort, without consumable accessory, the reliability of security and use all increases greatly, can realize long-period stable operation.
8, HY type gas retort reduced investment of the present invention, running cost are low.Use HY type gas retort without build supporting process furnace and corresponding thermal barrier delivery system for it, because its heat utilization rate is high, can realize destructive distillation heat self-balancing, therefore also without building producer gas generator and corresponding auxiliary facility, because its outlet is narrow-minded, so rear portion oil recovery system is also very simple.The construction investment of the destructive distillation oil refining factory of a same size is only 1/2 left and right of traditional destructive distillation factory.Due to the significantly minimizing of production equipment and power-equipment, power consumption, water consumption reduce, and running cost also will significantly reduce.
HY type gas retort of the present invention structurally takes following technical measures to realize the object of invention.The one, in destructive distillation chamber, be provided with carbonizing gas guidance device, solve carbonizing gas and passed through the excessive problem of the bed of material pressure-losses.After traditional technology carbonizing gas produces, rising, need to pass through the whole bed of material and just can discharge out of the furnace naturally, and drag losses is very large, thereby in stove, there will be that bias current, scaffold, obstruction, destructive distillation are inhomogeneous, even destructive distillation such as can not normally carry out at the phenomenon.And after HY type gas retort carbonizing gas produces, take the way that derives on the spot, carbonizing gas at most only need to pass through bed of material 1m, can enter carbonizing gas guidance device, smooth and easy arrival gas chamber.This has just guaranteed ventilative homogeneity in stove, and making becomes possibility to the destructive distillation of small particles material.The 2nd, combustion chamber is arranged to the both sides of destructive distillation chamber, directly to the heat supply of destructive distillation chamber, the heat lost by radiation of having avoided pipeline to carry thermal barrier, with regard to gas retort itself, except gas retort wall furnace wall has heat lost by radiation, destructive distillation subelement in the middle of gas retort does not have heat lost by radiation, does not more have pipeline to carry the heat lost by radiation of thermal barrier, the effective utilization that has so greatly improved heat.The 3rd, each destructive distillation unit is provided with two combustion chambers and two regenerator, by reversing valve alternate cycles, uses, and the application of heat storage technology has not only guaranteed the homeostasis of temperature of furnace wall, and funnel temperature is reduced to below 150 ℃, has improved thermo-efficiency.Gas retort of the present invention is compared with Fushun, Huadian formula gas retort, and the heat exhaustion of gas retort has reduced more than 50%.The 4th, in the bottom of gas retort, Semi-coke cooling device and cold burnt case are installed, pass into cold gas, by convective heat exchange, reclaim semicoke waste heat, be directly used in and supplement the needed heat of material destructive distillation.Although generally adopt the dry method technology of the discharging of the coke at coking industry at present, the heat reclaiming can not directly supplement the needs of destructive distillation heat, and the heat of this device recovery is directly used in destructive distillation itself.The 5th, HY type gas retort of the present invention top adopts through structure, has increased gas retort useful volume, and top is provided with a plurality of air chambers, by air chamber, collects carbonizing gas, and is provided with a plurality of relief outlets, and exhaust is more smooth and easy.Because flow area is large, the scale of construction of working off one's feeling vent one's spleen is few again, so gas retort exit gas flow velocity is little a lot of compared with Fushun, Huadian formula gas retort, has reduced micronic dust escaped quantity, has reduced greasy filth growing amount.The 6th, HY type gas retort of the present invention structurally adopts by a plurality of relatively independent destructive distillation subelements and combines, and each destructive distillation subelement can independent operating work.So just fundamentally solve the defect that Fushun, Huadian formula full circulation carbonization furnace can not amplify, be conducive to the realization that gas retort maximizes.Expand the treatment capacity of gas retort, as long as increase destructive distillation subelement.
Accompanying drawing explanation
Fig. 1 is HY type gas retort structure and process principle figure.In figure: 1, feed bin; 2, I slide valve; 3, hopper; 4, II push-pull valve; 5, preheating and drying chamber; 6, gas chamber; 7, destructive distillation chamber; 8, carbonizing gas guiding channel; 9, cooling room; 10, cold gas access tube; 11, cold gas blower; 12, cold burnt case; 13, keep off burnt plate; 14, coke extractor; 15, cold gas access tube; 16, water vapor access tube; 17, water coolant access tube; 18, burnt bucket; 19, III push-pull valve; 20, IV push-pull valve; 21, rotary conveyor; 22, carbonizing gas collecting tubule; 23, air chamber; 24, combustion chamber; 25, gas burner; 26, regenerator; 27, air enters pipe; 28, cigarette gas outlet pipe.
Fig. 2 is combustion chamber and regenerator fundamental diagram.In figure: 201, I combustion chamber; 202, II combustion chamber; 203, I combustion chamber burner; 204, II combustion chamber burner; 205, I regenerator; 206, II regenerator; 207, I regenerator smoke discharge tube; I 208, II regenerator smoke discharge tube; 209, I regenerator combustion air enters pipe; 210, II regenerator combustion air enters pipe; 211, I regenerator combustion air vent pipe; 212, II regenerator combustion air vent pipe; 213, fuel gas reversing valve; 214, combustion-supporting combustion air reversing valve; 215, combustion air gas blower; 216, fuel gas blower fan.
Fig. 3 is the HY type gas retort structural representation that has 3 destructive distillation subelements.
Embodiment
Accompanying drawing 1 is HY type gas retort fundamental diagram, shows that material adds from gas retort top, enters feed bin 1 in figure, I slide valve 2 is opened, and material enters hopper 3, while being full of material in hopper 3, close I slide valve 2, open II slide valve 4 under hopper, material relies on deadweight to fall in gas retort.When not reinforced, II slide valve 4 is in closing condition.This double disc baiting method can prevent that outer and stove outer air enters in stove by hopper furnace gas by hopper effusion stove.Material enters after gas retort, first by preheating and drying chamber 5, material is interior in preheating and drying chamber 5 is heated to 200 ℃～250 ℃ by the carbonizing gas of 500 ℃-550 ℃ from the 6 interior ejections of gas chamber, the moisture that material contains all evaporates, material continues to come downwards to the destructive distillation chamber 7 that both sides are combustion chamber furnace wall, material absorbs the radiations heat energy of both sides furnace wall in destructive distillation chamber, and temperature rises to 500 ℃～550 ℃, realizes complete destructive distillation.On the furnace wall of 7 both sides, destructive distillation chamber, have destructive distillation gas and derive passage 8, destructive distillation gas is derived passage 8 and gas chamber 6 communicates.Semicoke after destructive distillation continues descending through cooling room 9, cooling room 9 both sides are provided with cold gas and enter pipe 10 and cold gas blower 11, semicoke is cooled to 150 ℃～200 ℃ by the cold gas of 35 ℃-40 ℃ of ejection from cold gas blower 11, material enters cold burnt case 12, in cold burnt case, be provided with the burnt plate 13 of gear, coke extractor 14, cold gas access tube 15, water vapour access tube 16, water coolant access tube 17, the cold gas spraying into, water vapour and water coolant continue cooling to material, water vapour also plays the effect of sealing gland simultaneously in addition, prevent that top gas is from the bottom effusion of cold burnt case, material baffle 13 can swing, control the gap of discharge, prevent that in stove, the phenomenon of coming to nothing appears in material, coke extractor 14 enters the semicoke after destructive distillation burnt bucket 18 in rotation process, semicoke is cooled to 100 ℃ of following discharges in cold burnt case, in burnt bucket 18, be provided with two slide valves, it is top III slide valve 19, bottom IV slide valve 20, not during discharge, III slide valve 19 is opened, IV slide valve 20 cuts out, during discharge, III slide valve 19 cuts out, and IV slide valve 20 is opened, material is arranged at cold burnt lower box part rotary conveyor 21 after discharging is transported to stockyard.In the destructive distillation chamber 7 of gas retort, be provided with independently carbonizing gas guidance device, carbonizing gas guidance device is comprised of carbonizing gas guiding channel 8 and gas chamber 6, the carbonizing gas producing in retort process, and the cold gas passing into from gas retort bottom imports gas chamber 6 through carbonizing gas guiding channel 8, from gas chamber ejection through preheating and drying chamber 5, carbonizing gas transfers heat to the material that has just added gas retort in uphill process, self temperature constantly declines, to air chamber 23 places that are arranged at gas retort top, temperature is 90 ℃～110 ℃, discharge out of the furnace, through gas manifold 22, be sent to oil recovery system.Carbonizing gas is being cooled to 35 ℃～40 ℃ through reclaiming the oily substance wherein containing after separated moisture, and a part is sent into combustion chamber 24 by gas blower fan and used as fuel, and a part enters gas retort bottom for cooling semicoke.The both sides of destructive distillation chamber 7 are combustion chamber 24, and bottom, combustion chamber is provided with fuel gas and enters pipe 25, and regenerator 26, is equipped with heat storage in regenerator, and regenerator is provided with air and enters pipe 27 and smoke discharge tube 28.Air blasts regenerator by gas blower and is preheating to more than 500 ℃, mix with fuel gas again, in combustion chambers burn, the high-temperature flue gas that burning produces is 900 ℃～1000 ℃, both sides furnace wall is heated to more than 700 ℃, high-temperature flue gas enters the regenerator of opposite side, and by thermal exchange, to heat storage, flue-gas temperature is lowered to 150 ℃ of following rear discharges.
Fig. 2 is the principle of work schematic diagram of combustion chamber and regenerator.This device is provided with two combustion chambers, two regenerator, alternate cycles is used, with the temperature all-the-time stable that guarantees both sides, combustion chamber furnace wall more than 700 ℃.Gas burner is installed in combustion chamber, in regenerator, fills heat storage.The furnace wall of two combustion chambers is passed to heat by destructive distillation material by radiation, by heating material to 500 ℃～550 ℃, makes material generation destructive distillation.Operating mode shown in figure is that I combustion chamber 201 is in burning; I regenerator 205 is providing combustion air; II regenerator 206 is in accumulation of heat; Exhaust gases passes is used as in II combustion chamber 202.Implementation process is: combustion air enters pipe 209 by gas blower 214 through combustion air and blasts I regenerator 205, and absorb the heat of heat storage, combustion air is preheating to more than 500 ℃ in I regenerator, through combustion air vent pipe 211 and fuel gas, mix, gas burner 203 ejection burnings in being located at I combustion chamber, the high-temperature flue gas that burning produces is 900 ℃～1000 ℃, furnace wall is heated to more than 700 ℃, high-temperature flue gas enters II regenerator 206, by thermal exchange, to heat storage, flue-gas temperature is lowered to 150 ℃ and from smoke discharge tube 208, discharges after following.After the first loop ends, 214 commutations of combustion air reversing valve.Combustion air enters II regenerator, and absorb the heat of heat storage, air is preheating to more than 500 ℃, mix with fuel gas, in II combustion chamber, burn, the high-temperature flue gas that burning produces is 900 ℃～1000 ℃, furnace wall is heated to more than 700 ℃, high-temperature flue gas enters I regenerator, and by thermal exchange, to heat storage, flue-gas temperature is lowered to 150 ℃ of following rear discharges.So go round and begin again, form continuous technique.
Fig. 3 is structure and the fundamental diagram that has the HY type gas retort of 3 destructive distillation subelements.As shown in the figure, the preheating and drying chamber, top of the gas retort that a plurality of destructive distillation subelements form is communicated with, and air-flow and material can unrestricted flows.Each corresponding destructive distillation chamber of both sides, the combustion chamber furnace wall of middle destructive distillation unit, separates with combustion chamber between two destructive distillation unit.
Implement HY type gas retort of the present invention and should be noted that following problem: 1, the quantity of destructive distillation subelement is set according to the processing power decision of the needs of gas retort, the processing power of gas retort is directly proportional with the quantity that destructive distillation subelement is set.Although each destructive distillation subelement can independent operating, due in order to guarantee even destructive distillation, destructive distillation subelement narrower in width, is generally no more than 0.6m.The daily handling ability of the destructive distillation subelement that sectional area is 1000mm * 4000mm is about 50～100 tons of left and right.2, the daily handling ability of the gas retort of same specification, with relevant by factors such as the character of destructive distillation material, water content, maximum particle diameter, particle diameter ratio, destructive distillation final temperature, destructive distillation caloric receptivities, need be adjusted according to practical situation.In general, when material moisture is low, particle diameter is little, destructive distillation final temperature is low, the treatment capacity of destructive distillation caloric receptivity hour gas retort is larger, otherwise treatment capacity is smaller.While 3, using HY type gas retort of the present invention, be the permeability that guarantees material in stove, to entering the maximum particle diameter of material of gas retort destructive distillation and the ratio of minimum grain size, be advisable between being controlled at 2～3.While 4, using HY type gas retort of the present invention, the size of the cold gas amount passing into is reduced between 120 ℃～150 ℃ and is advisable with control semicoke temperature.5, HY type gas retort of the present invention is applicable to the material below destructive distillation 50mm.The material larger to particle need first carry out fragmentation, to the HY type of the present invention of the material below the 12mm going out of use in traditional distillation process gas retort, can utilize.6, the concrete installation site of gas retort internal part and structure should meet the requirement that realizes the complete destructive distillation of material, otherwise the permeability of gas retort and the degree that material reaches complete destructive distillation in gas retort will be affected, even will cause carbonizing gas to derive difficulty, affect oil recovery rate, affect the thermo-efficiency of gas retort.As the distance that cold gas spout is derived passage to carbonizing gas, between 1.5-2m, select, the height of preheating and drying section is selected between 1.5-2.5m.
Claims (5)
1. a HY type gas retort, its constitutional features is: gas retort is comprised of a plurality of destructive distillation subelements, each destructive distillation subelement is comprised of feeding device, oil gas discharger, destructive distillation device, heating unit, discharging device for coke;
Described feeding device is arranged at the top of gas retort, by feed bin, hopper, two slide valves, formed, wherein first slide valve is arranged between feed bin and hopper, and second slide valve is arranged at hopper bottom, and hopper communicates through the preheating and drying chamber of second slide valve and destructive distillation device;
Described oil gas discharger is arranged at the top of destructive distillation device, air chamber and carbonizing gas collecting tubule, consists of; The preheating and drying chamber of air chamber bottom and destructive distillation device communicates, and top is connected with carbonizing gas collecting tubule;
Described destructive distillation device is comprised of preheating and drying chamber, destructive distillation chamber, cooling room, carbonizing gas guidance device; Preheating and drying chamber, destructive distillation chamber, cooling room are arranged in order from top to bottom; The furnace wall that wherein both sides, destructive distillation chamber are combustion chamber; Carbonizing gas guidance device is comprised of carbonizing gas guiding channel and gas chamber, carbonizing gas guiding channel is arranged in the furnace wall of combustion chamber, gas chamber is arranged at the top of combustion chamber, and carbonizing gas guiding channel and gas chamber communicate, and gas chamber is provided with carbonizing gas ejiction opening; Cooling room is arranged at the bottom of destructive distillation chamber, and cooling room both sides are provided with cold gas and enter pipe and cold gas spout, and cooling room bottom and cold burnt case communicate;
Described heating unit enters pipe, gas burner, preheated air by combustion chamber, regenerator, fuel gas and enters pipe, and smoke discharge tube, reversing valve, combustion air gas blower, smoke evacuation induced draft fan, fuel gas blower fan form; The heating unit of a unit is provided with two combustion chambers, two regenerator; Combustion chamber is arranged at the both sides of destructive distillation chamber, and gas burner is arranged in combustion chamber, and gas burner enters pipe with fuel gas, fuel gas blower fan is connected successively; Regenerator is arranged at combustion chamber lower outside, and heat storage is housed in regenerator, and regenerator is provided with preheated air and enters pipe, and smoke discharge tube is connected with combustion air gas blower, smoke evacuation induced draft fan respectively; Fuel gas enters pipe and preheated air and enters reversing valve is installed on pipe;
Described discharging device for coke constitutional features is: discharging device for coke is arranged at gas retort bottom, cold burnt case, coke extractor, the burnt plate of shelves, cold gas access tube, steam access tube, water coolant access tube, two slide valves and rotary conveyor, consists of; Coke extractor, the burnt plate of shelves are arranged in cold burnt case, and cold burnt casing is provided with cold gas access tube, steam access tube, water coolant access tube, and cold burnt lower box part is provided with two slide valves and rotary conveyor.
2. HY type gas retort according to claim 1, its constitutional features is: gas retort is comprised of a plurality of destructive distillation subelements; The preheating and drying section on the gas retort top that a plurality of destructive distillation subelements form is interconnected; Each corresponding destructive distillation chamber of both sides, the combustion chamber furnace wall of middle destructive distillation unit, separates with combustion chamber between two destructive distillation unit.
3. HY type gas retort according to claim 1, be applicable to in oil-sand, resinous shale and coal, low-temperature pyrolysis oil refining.
4. HY type gas retort according to claim 1, be applicable to in large granular materials, low-temperature pyrolysis oil refining.
5. HY type gas retort according to claim 1, be applicable to be less than 15mm material in, low-temperature pyrolysis oil refining.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201420185555.3U CN203794835U (en) | 2014-04-17 | 2014-04-17 | HY type dry distillation furnace |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201420185555.3U CN203794835U (en) | 2014-04-17 | 2014-04-17 | HY type dry distillation furnace |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103923676A (en) * | 2014-04-17 | 2014-07-16 | 沈阳海源干馏设备技术开发有限公司 | HY type dry distillation furnace |
| CN104762096A (en) * | 2015-03-31 | 2015-07-08 | 长安大学 | Gas guide unit, gas guide device, coal powder pyrolysis device and coal powder pyrolysis method |
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2014
- 2014-04-17 CN CN201420185555.3U patent/CN203794835U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103923676A (en) * | 2014-04-17 | 2014-07-16 | 沈阳海源干馏设备技术开发有限公司 | HY type dry distillation furnace |
| CN103923676B (en) * | 2014-04-17 | 2015-06-03 | 吴冠峰 | HY type dry distillation furnace |
| CN104762096A (en) * | 2015-03-31 | 2015-07-08 | 长安大学 | Gas guide unit, gas guide device, coal powder pyrolysis device and coal powder pyrolysis method |
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