CN102757805B - Low-temperature dry distillation equipment and method of low-rank coal and oil shale and petroleum residue - Google Patents
Low-temperature dry distillation equipment and method of low-rank coal and oil shale and petroleum residue Download PDFInfo
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- CN102757805B CN102757805B CN 201210187990 CN201210187990A CN102757805B CN 102757805 B CN102757805 B CN 102757805B CN 201210187990 CN201210187990 CN 201210187990 CN 201210187990 A CN201210187990 A CN 201210187990A CN 102757805 B CN102757805 B CN 102757805B
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Abstract
The invention provides low-temperature dry distillation equipment and method of low-rank coal and oil shale and petroleum residue. The equipment comprises a gas retort gyring main engine, a material and heating porcelain ball mixing spiral feeding machine, and a gas-solid separating box, wherein the material and heating porcelain ball mixing spiral feeding machine is connected with a material inlet end of the gas retort gyring main engine; the gas-solid separating box is connected with a material outlet end of the gas retort gyring main engine; the gas retort gyring main engine adopts a cylindrical structure which is downward obliquely arranged from the material inlet end to the material outlet end; an internal cylinder is arranged at the middle axis of an external cylinder of the dry distillation gyring main engine; and the internal cylinder and the external cylinder are integrally connected from the material inlet end to the material outlet end through a plurality of arc-shaped plates which are axially distributed. The low-temperature dry distillation equipment provided by the invention has the advantages of simple structure, high processing output, heat transfer performance, high efficiency, energy conservation and high purity of gas under dry distillation, can be widely used for low-temperature dry distillation on low-grade fossil energy such as various low-rank coal, low-rank oil shale and petroleum residue, and can produce high-grade products such as coal, coke, shale oil and semi-coke.
Description
Technical field
The invention belongs to low-temperature pyrolysis equipment and the low-temperature cracking process in derived energy chemical field, particularly a kind of low-grade fossil energy.
Background technology
Thereby destructive distillation generally refers to solid organic matters and heat the process that pyrolytic reaction takes place under the state of secluding air, be broadly divided into low temperature, middle temperature, high temperature and ultrahigh-temperature destructive distillation according to different Heating temperatures, the industrial coal carbonization that is usually used in, and adopt low-temperature pyrolysis (500～650 ℃) can be widely used in low-rank coal and low-grade fossil energy such as resinous shale, petroleum residue, its product can obtain tar and the coal gas of high yield, and the remaining solid thing is that height contains the charcoal semicoke.Distillation process is for the treatment of existing very long history such as coal, resinous shale and petroleum residue, be example with the coal, its pyrogenation and carbonization technology started from for 20 beginnings of the century, low-temperature pyrolysis (pyrolysis) method for upgrading that once occurred a lot of coals in history, but having only of industrial achieving success is several, these methods are divided into outside external-heat, internal heat type and the interior heat hot hybrid by the type of heating of stove, can be divided into gaseous heat-carrier, solid thermal carriers mode again according to heating medium, whether contact with material and be divided into direct heating and indirect heating mode according to heating medium.
The 1950's, along with exploitation and the application of world wide oil, Sweet natural gas, pyrolysis of coal technological development speed slows down even pauses, but in the abundant country of some coal resources, never is interrupted the research and development to pyrolysis of coal.The seventies in 20th century, owing to three oil crisises in the world with to the clean energy growth of requirement, cause the attention to low-rank coal and resinous shale equal energy source pyrogenation and carbonization once again.Along with people pay attention to again to the research and development of pyrolysis of coal technology, develop some novel procesies successively.These novel procesies are directly burnt with coal and are compared, can produce the product of three kinds of different shapes of gas, liquid, solid, be actually heterogeneity in the coal is carried out the utilization of branch matter, in the pyrolysis product: hydrogenation of tar can be produced petroleum supplements and refinery cokes such as gasoline, diesel oil, residual oil; Coal gas can be used as the unstripped gas of clean fuel and inhibition and generation worker synthetic gas; Semicoke is the high-quality smokeless fuel, can be used as domestic fuel and calcium carbide, iron alloy, iron-smelting blast furnace blowing material, also is gasification raw material, the sorbing material of high-quality.Therefore the pyrogenation and carbonization of coal is the effective ways of the clean high-efficiency comprehensive utilization of coal, both can reduce the environmental pollution that fire coal causes, can improve low-rank coal comprehensive utilization of resources rate and value-added content of product again, have remarkable economic efficiency and environmental benefit, meet national industrial policies.
Abroad, states such as U.S., day, moral, Australia have extensively carried out research and test work, handle 1000 tons brown coal drying destructive distillation industry demonstration unit in one cover day of Wyoming State Gillette town Buckskin construction of coal mine as USDOE approval in 1989 and subsidy, go into operation in June, 1992, nearly 5 years have been moved, the liquid product that extracts from coal (CDL) is as oil replacement fuel, among the commercialization factory that year processing coal is 3,000,000 tons is designing and building.The Coalcon company of U.S. combinating carbide company has developed advanced on-catalytic hydropyrolysis technology, and pyrolysis temperature is 560 ℃, and hydrogenation pressure is up to 6.9MPa, and its liquids and gases productive rate height, product separate easily.
China begins to carry out the R and D work of pyrolysis of coal technology the 1950's.Units such as petroleum institute, Beijing, Dalian University of Technology, Zhejiang University, Shanxi coalification institute of the Chinese Academy of Sciences, Beijing coalification institute, Shaanxi coal industry chemical industry group have successively developed the pyrolysis of coal technology of different process, and have set up the large scale industry device.Beginning to build up a collection of at the beginning of the area, Yulin 90 is the internal heat type block furnace long-flame coal lump coal gas retort of representative with three river coalification companies, from single stove ability 3～50,000 ton/year, develop into present single stove ability 7.5～100,000 ton/year, the large-scale gas retort that single stove is 200,000 tons/year also puts into operation, has succeeded in developing the type of furnaces such as externally heated retort oven, two-part gas retort simultaneously.Total capacity reaches more than 2,600 ten thousand tons.
Less with respect to coal for the pyrogenation and carbonization technical study of resinous shale and petroleum residue both at home and abroad, but present stage be based on low-temperature pyrolysis.
At present, exist more than 20 kind of low-temperature pyrolysis both at home and abroad, various technology respectively have relative merits, and existing apparatus and technology exist mostly that efficiency ratio, low, the oily yield of gas production rate quality are low, poor stability, energy dissipation, cost are crossed problems such as height, and the assistant officer is to be solved.
Summary of the invention
The invention provides a kind of low-temperature pyrolysis Apparatus and method for for low-rank coal, resinous shale, petroleum residue, solve that little, the oily yield of low, the single covering device output of poor stability, efficiency ratio, gas production rate quality that existing low-temperature pyrolysis Apparatus and method for exists is low, energy dissipation, production cost cross high technical problem.
The technical solution adopted for the present invention to solve the technical problems is:
This low-temperature pyrolysis equipment for low-rank coal, resinous shale, petroleum residue, constituted by gas retort revolution main frame, material and heating porcelain ball mixing auger feeding machine, gas solid separation case three parts, material and heating porcelain ball mixing auger feeding machine are connected with the feed end of gas retort revolution main frame, and the gas solid separation case is connected with the discharge end of gas retort revolution main frame;
Described gas retort revolution main frame is the tubular structure from feed end to the downward-sloping layout of discharge end; The urceolus axis of gas retort revolution main frame is provided with inner core, the arc of being arranged vertically by polylith from feed end to discharge end between inner core and the urceolus links together, arc to feed end before the gas retort revolution main frame discharge end is the forward arc that positive rotation direction is installed, the forward arc distributes on the cross section of gas retort revolution main frame radially, be configured for storing the pyrolysis reaction region point compartment of material and porcelain ball, the arc of gas retort revolution main frame discharge end is that derotation is to the inverse-arc shape plate of installing, the inverse-arc shape plate distributes on the cross section of gas retort revolution main frame radially, constitutes discharge zone and divides compartment;
Described gas retort revolution main frame is by main motor, main gear reducer, pinion(gear) and master wheel driven rotary, master wheel is connected outer drum outer wall, revolution is supported by sliding end rolling ring, sliding end lateral part wheel and sliding end support roller in the urceolus front portion, and revolution is supported by inboardend rolling ring, inboardend lateral part wheel and inboardend support roller in the urceolus rear portion;
The front end of described gas retort revolution main frame is provided with the charging end plate, and charging end plate center is connected with the charging quill shaft, and gas retort revolution host back end is provided with the discharging end plate, and discharging end plate center is connected with the discharging quill shaft;
Described material and heating porcelain ball mixing auger feeding machine comprise feeding serew, feeding serew casing, feeding serew drive-motor, material elephant trunk and porcelain ball elephant trunk; Feeding serew is installed on feeding serew casing inside, the feeding serew front end drives rotation by the feeding serew drive-motor, in the cavity of terminal insertion gas retort revolution main frame, feeding serew casing rear portion is connected by the charging quill shaft of feed end seal head with gas retort revolution main frame, feeding serew casing end face is having feeding mouth with the anterior corresponding position of feeding serew, and the material elephant trunk is connected with feeding mouth with porcelain ball elephant trunk simultaneously;
Described gas solid separation case comprises gas solid separation case body, the outlet of destructive distillation gas and semicoke and porcelain ball discharging blocking valve, the feeding mouth of gas solid separation case body side is connected by the discharging quill shaft of discharge end seal head with gas retort revolution main frame, gas solid separation case bodies top is located in the outlet of destructive distillation gas, and semicoke and porcelain ball discharging blocking valve are located at gas solid separation case body bottom.
Described charging quill shaft inwall has the charging internal screw, and discharging quill shaft inwall has the discharging internal screw.
The inner side edge of described arc is connected with inner tank theca by the inner core articulated slab, and outer side edges is connected with outer tube inner wall by the urceolus articulated slab.
The bottom of described feeding serew casing and feeding serew drive-motor is seated on the feeding serew walking basal seat, and the feeding serew walking basal seat is walked on the feed end guide rail by roller.
The bottom of described gas solid separation case body is seated on the separator box movable base, and the separator box movable base is walked on the discharge end guide rail by roller.
Described outer drum outer wall is enclosed with one deck refractory materials.
Be connected with expansion joint on the feeding mouth of described material and heating porcelain ball mixing auger feeding machine, the material elephant trunk is connected with feeding mouth through expansion joint with porcelain ball elephant trunk simultaneously.
Described feeding serew drive-motor and main motor are variable-frequency motor.
This employing is used for low-rank coal, resinous shale, the low-temperature cracking process of the low-temperature pyrolysis equipment of petroleum residue, material and heated porcelain ball enter the feeding mouth of material and heating porcelain ball mixing auger feeding machine respectively by material elephant trunk and porcelain ball elephant trunk, feeding serew rotates under the drive of feeding serew drive-motor, material and hot porcelain ball are mixed and push in the cavity of gas retort revolution main frame, and enter into different pyrolysis reaction region respectively with the rotation of gas retort revolution main frame and divide in the compartment, on the cross section of gas retort revolution main frame, store in each pyrolysis reaction region point compartment and go up material and hot porcelain ball, material and hot porcelain ball are along with the abundant hybrid concurrency of revolution of gas retort revolution main frame is given birth to heat exchange, material heats up and pyrolytic reaction takes place, hot porcelain ball is then lowered the temperature chemical reaction is not taken place, carbonizing gas is separated out and is derived backward from the cavity upper space of gas retort revolution main frame, enter at last in the gas solid separation case, material in the pyrolysis reaction region point compartment and porcelain ball under the effect of gravity constantly by moving to low level from a high position, the discharge zone that is pooled to afterbody at last divides in the compartment, material and the porcelain ball of having put heat are promoted in the discharging quill shaft to the inverse-arc shape plate of installing by derotation in the discharge zone point compartment, again in the discharging quill shaft enters gas solid separation case body, material and soft-paste ball sink down into semicoke and porcelain ball discharging blocking valve in gas solid separation case body, semicoke and porcelain ball discharging blocking valve only allow solid materials and porcelain ball to discharge and do not allow carbonizing gas to discharge, and carbonizing gas is discharged by the destructive distillation gas outlet of gas solid separation box top.
Beneficial effect of the present invention is as follows:
The compartment that gas retort revolution main frame of the present invention inside distributes radially can be used for storing material and porcelain ball, and the pyrolysis space of material is provided simultaneously.Adopt a plurality of compartments to increase the interior stacking factor of gas retort, improved stand-alone device output.Material in the compartment directly contacts with the porcelain ball, and fully mixes stirring with the rotation of cylindrical shell in compartment, and thermal conduction is fast, the heat exchange efficiency height.Arc derotation in the gas retort revolution main frame afterbody compartment can and have been put hot porcelain ball with material and be promoted in the discharging quill shaft to installation, is furnished with the discharging internal screw in the quill shaft, can in rotating process material and porcelain ball be unloaded to the gas solid separation case.Gas retort is owing to adopt the porcelain ball to add thermal material as thermal barrier, and porcelain ball itself can not produce other flue gas class materials, and material is heated the back destructive distillation gas of separating out and does not contain other impurity, and the gas purity height is applicable to the raw material as Coal Chemical Industry.Whole gas retort whole set adopts refractory materials to do insulation, and heat scatters and disappears few, and is energy-conservation.
Gas retort revolution main frame and feeding serew rotate by separately variable-frequency motor and actuator drives, thereby realize lifting and the propelling of material and porcelain ball.Owing to adopt variable-frequency motor, so feeding capacity and gas retort cylindrical shell velocity of rotation are all adjustable, and equipment has good modulability, can adapt to different materials, and is controlled good.
Material and heating porcelain ball mixing auger feeding machine and gas-solid separator box are equipped with the base of walking on guide rail, and when equipment generation thermal expansion, base can be mobile at guide rail, thereby have improved security and the controllability of equipment.
Low-temperature pyrolysis simple in equipment of the present invention, handle that output is big, heat-exchange efficient energy-saving, carbonizing gas purity height, the low-temperature pyrolysis of low-grade fossil energies such as all kinds of low-rank coal (as: brown coal, long-flame coal, non-caking coal, weakly caking coal) and resinous shale, petroleum residue can be widely used in, products such as high-grade coal gas, tar, shale oil, semicoke can be obtained.
Description of drawings
The present invention is further described below in conjunction with drawings and Examples.
Fig. 1 is structural representation of the present invention.
Fig. 2 is the structural representation of Figure 1A-A section.
Fig. 3 is the structural representation of Figure 1B-B section.
Fig. 4 is that gas retort revolution main frame divides compartment and discharge zone to divide the structural representation of compartment intersection in pyrolysis reaction region.
Reference numeral: 1-feed end guide rail, 2-feeding serew walking basal seat, 3-feeding serew drive-motor, the 4-feeding serew, the 5-expansion joint, 6-material elephant trunk, 7-porcelain ball elephant trunk, 8-feed end seal head, 9-charging quill shaft, 10-charging end plate, 11-forward arc, 12-urceolus articulated slab, the rolling ring of 13-sliding end, the 14-urceolus, 15-inner core articulated slab, the 16-inner core, the 17-master wheel, the rolling ring of 18-inboardend, 19-inverse-arc shape plate, 20-discharging end plate, 21-discharge end seal head, the outlet of 22-destructive distillation gas, 23-discharge end guide rail, 24-separator box movable base, 25-semicoke and porcelain ball discharging blocking valve, 26-gas solid separation case body, 27-discharging quill shaft, 28-inboardend lateral part wheel, 29-inboardend support roller, 30-master's motor, the 31-main gear reducer, the 32-pinion(gear), 33-sliding end lateral part wheel, 34-sliding end support roller, the 35-refractory materials, 37-feeding serew casing, the 38-pyrolysis reaction region is divided compartment, the 39-discharge zone divides compartment.
Embodiment
Embodiment is referring to shown in Figure 1, this low-temperature pyrolysis equipment for low-rank coal, resinous shale, petroleum residue, constituted by gas retort revolution main frame, material and heating porcelain ball mixing auger feeding machine, gas solid separation case three parts, material and heating porcelain ball mixing auger feeding machine are connected with the feed end of gas retort revolution main frame, and the gas solid separation case is connected with the discharge end of gas retort revolution main frame.
Described gas retort revolution main frame is the tubular structure from feed end to the downward-sloping layout of discharge end; Urceolus 14 outer walls of gas retort revolution main frame are enclosed with one deck refractory materials 35, urceolus 14 axis of gas retort revolution main frame are provided with inner core 16, the arc of being arranged vertically by polylith from feed end to discharge end between inner core 16 and the urceolus 14 links together, the inner side edge of arc is connected with inner core 16 outer walls by inner core articulated slab 15, outer side edges is connected with urceolus 14 inwalls by urceolus articulated slab 12, arc to feed end before the gas retort revolution main frame discharge end is the forward arc 11 that positive rotation direction is installed, forward arc 11 distributes on the cross section of gas retort revolution main frame radially, be configured for storing the pyrolysis reaction region point compartment 38 of material and porcelain ball, the arc of gas retort revolution main frame discharge end is that derotation is to the inverse-arc shape plate of installing 19, inverse-arc shape plate 19 distributes on the cross section of gas retort revolution main frame radially, constitutes discharge zone and divides compartment 39.
Described gas retort revolution main frame is by main motor 30, main gear reducer 31, pinion(gear) 32 and master wheel 17 driven rotary, master wheel 17 is connected urceolus 14 outer walls, revolution is supported by sliding end rolling ring 13, sliding end lateral part wheel 33 and sliding end support roller 34 in urceolus 14 front portions, revolution is supported by inboardend rolling ring 18, inboardend lateral part wheel 28 and inboardend support roller 29 in urceolus 14 rear portions, and main motor 30 is variable-frequency motor.
The front end of described gas retort revolution main frame is provided with charging end plate 10, charging end plate 10 centers are connected with charging quill shaft 9, charging quill shaft 9 inwalls have the charging internal screw, gas retort revolution host back end is provided with discharging end plate 20, discharging end plate 20 centers are connected with discharging quill shaft 27, and discharging quill shaft 27 inwalls have the discharging internal screw.
Described material and heating porcelain ball mixing auger feeding machine comprise feeding serew 4, feeding serew casing 37, feeding serew drive-motor 3, material elephant trunk 6 and porcelain ball elephant trunk 7; Feeding serew 4 is installed on feeding serew casing 37 inside, feeding serew 4 front ends drive rotation by feeding serew drive-motor 3, feeding serew drive-motor 3 is variable-frequency motor, in the cavity of feeding serew 4 terminal insertion gas retort revolution main frames, feeding serew casing 37 rear portions are connected by the charging quill shaft 9 of feed end seal head 8 with gas retort revolution main frame, feeding serew casing 37 end faces are having feeding mouth with feeding serew 4 anterior corresponding positions, be connected with expansion joint 5 on the feeding mouth, material elephant trunk 6 is connected with feeding mouth through expansion joint 5 with porcelain ball elephant trunk 7 simultaneously, feeding serew casing 37 is seated on the feeding serew walking basal seat 2 with the bottom of feeding serew drive-motor 3, and feeding serew walking basal seat 2 is walked on the feed end guide rail 1 by roller.
Described gas solid separation case comprises gas solid separation case body 26, the outlet 22 of destructive distillation gas and semicoke and porcelain ball discharging blocking valve 25, the feeding mouth of gas solid separation case body 26 sides is connected by the discharging quill shaft 27 of discharge end seal head 21 with gas retort revolution main frame, gas solid separation case body 26 tops are located in destructive distillation gas outlet 22, semicoke and porcelain ball discharging blocking valve 25 are located at gas solid separation case body 26 bottoms, the bottom of gas solid separation case body 26 is seated on the separator box movable base 24, and separator box movable base 24 is walked on the discharge end guide rail 23 by roller.
Referring to Fig. 2, described forward arc 11 distributes on the cross section of gas retort revolution main frame radially, constitutes pyrolysis reaction region and divides compartment 38.
Referring to Fig. 3, described inverse-arc shape plate 19 distributes on the cross section of gas retort revolution main frame radially, constitutes discharge zone and divides compartment 39.
Referring to Fig. 4, described gas retort revolution main frame divides compartment and discharge zone to divide the compartment intersection in pyrolysis reaction region, and forward arc 11 arranges for rotation direction is opposite with inverse-arc shape plate 19.
This employing is used for low-rank coal, resinous shale, the low-temperature cracking process of the low-temperature pyrolysis equipment of petroleum residue, material and heated porcelain ball enter the feeding mouth of material and heating porcelain ball mixing auger feeding machine respectively by material elephant trunk 6 and porcelain ball elephant trunk 7, feeding serew 4 rotates under the drive of feeding serew drive-motor 3, material and hot porcelain ball are mixed and push in the cavity of gas retort revolution main frame, and enter into different pyrolysis reaction region respectively with the rotation of gas retort revolution main frame and divide in the compartment 38, on the cross section of gas retort revolution main frame, store in each pyrolysis reaction region point compartment 38 and go up material and hot porcelain ball, material and hot porcelain ball are along with the abundant hybrid concurrency of revolution of gas retort revolution main frame is given birth to heat exchange, material heats up and pyrolytic reaction takes place, hot porcelain ball is then lowered the temperature chemical reaction is not taken place, carbonizing gas is separated out and is derived backward from the cavity upper space of gas retort revolution main frame, enter at last in the gas solid separation case, material in the pyrolysis reaction region point compartment 38 and porcelain ball under the effect of gravity constantly by moving to low level from a high position, the discharge zone that is pooled to afterbody at last divides in the compartment 39, material and the porcelain ball of having put heat are promoted in the discharging quill shaft 27 to the inverse-arc shape plate of installing 19 by derotation in the discharge zone point compartment 39, again in discharging quill shaft 27 enters gas solid separation case body 26, material and soft-paste ball sink down into semicoke and porcelain ball discharging blocking valve 25 in gas solid separation case body 26,25 of semicoke and porcelain ball discharging blocking valves allow solid materials and porcelain ball to discharge and do not allow carbonizing gas to discharge, and carbonizing gas is discharged by the destructive distillation gas outlet 22 of gas solid separation box top.
Claims (7)
1. low-temperature pyrolysis equipment that is used for low-rank coal, resinous shale, petroleum residue, it is characterized in that: constituted by gas retort revolution main frame, material and heating porcelain ball mixing auger feeding machine, gas solid separation case three parts, material and heating porcelain ball mixing auger feeding machine are connected with the feed end of gas retort revolution main frame, and the gas solid separation case is connected with the discharge end of gas retort revolution main frame;
Described gas retort revolution main frame is the tubular structure from feed end to the downward-sloping layout of discharge end; Urceolus (14) axis of gas retort revolution main frame is provided with inner core (16), the arc of being arranged vertically by polylith from feed end to discharge end between inner core (16) and the urceolus (14) links together, arc to feed end before the gas retort revolution main frame discharge end is the forward arc (11) that positive rotation direction is installed, forward arc (11) distributes on the cross section of gas retort revolution main frame radially, be configured for storing the pyrolysis reaction region point compartment (38) of material and porcelain ball, the arc of gas retort revolution main frame discharge end is that derotation is to the inverse-arc shape plate of installing (19), inverse-arc shape plate (19) distributes on the cross section of gas retort revolution main frame radially, constitutes discharge zone and divides compartment (39);
Described gas retort revolution main frame is by main motor (30), main gear reducer (31), pinion(gear) (32) and master wheel (17) driven rotary, master wheel (17) is connected urceolus (14) outer wall, urceolus (14) is anterior to support revolution by sliding end rolling ring (13), sliding end lateral part wheel (33) and sliding end support roller (34), and revolution is supported by inboardend rolling ring (18), inboardend lateral part wheel (28) and inboardend support roller (29) in urceolus (14) rear portion;
The front end of described gas retort revolution main frame is provided with charging end plate (10), charging end plate (10) center is connected with charging quill shaft (9), gas retort revolution host back end is provided with discharging end plate (20), and discharging end plate (20) center is connected with discharging quill shaft (27);
Described material and heating porcelain ball mixing auger feeding machine comprise feeding serew (4), feeding serew casing (37), feeding serew drive-motor (3), material elephant trunk (6) and porcelain ball elephant trunk (7); Feeding serew (4) is installed on feeding serew casing (37) inside, feeding serew (4) front end drives rotation by feeding serew drive-motor (3), in the cavity of terminal insertion gas retort revolution main frame, feeding serew casing (37) rear portion is connected by the charging quill shaft (9) of feed end seal head (8) with gas retort revolution main frame, feeding serew casing (37) end face is having feeding mouth with the anterior corresponding position of feeding serew (4), and material elephant trunk (6) is connected with feeding mouth with porcelain ball elephant trunk (7) simultaneously;
Described gas solid separation case comprises gas solid separation case body (26), the outlet of destructive distillation gas (22) and semicoke and porcelain ball discharging blocking valve (25), the feeding mouth of gas solid separation case body (26) side is connected by the discharging quill shaft (27) of discharge end seal head (21) with gas retort revolution main frame, gas solid separation case body (26) top is located in destructive distillation gas outlet (22), and semicoke and porcelain ball discharging blocking valve (25) are located at gas solid separation case body (26) bottom;
Described charging quill shaft (9) inwall has the charging internal screw, and discharging quill shaft (27) inwall has the discharging internal screw;
The inner side edge of described arc is connected with inner core (16) outer wall by inner core articulated slab (15), and outer side edges is connected with urceolus (14) inwall by urceolus articulated slab (12).
2. the low-temperature pyrolysis equipment for low-rank coal, resinous shale, petroleum residue according to claim 1, it is characterized in that: described feeding serew casing (37) is seated on the feeding serew walking basal seat (2) with the bottom of feeding serew drive-motor (3), and feeding serew walking basal seat (2) is walked on the feed end guide rail (1) by roller.
3. the low-temperature pyrolysis equipment for low-rank coal, resinous shale, petroleum residue according to claim 1, it is characterized in that: the bottom of described gas solid separation case body (26) is seated on the separator box movable base (24), and separator box movable base (24) is walked on the discharge end guide rail (23) by roller.
4. the low-temperature pyrolysis equipment for low-rank coal, resinous shale, petroleum residue according to claim 1, it is characterized in that: described urceolus (14) outer wall is enclosed with one deck refractory materials (35).
5. the low-temperature pyrolysis equipment for low-rank coal, resinous shale, petroleum residue according to claim 1, it is characterized in that: be connected with expansion joint (5) on the feeding mouth of described material and heating porcelain ball mixing auger feeding machine, material elephant trunk (6) is connected with feeding mouth through expansion joint (5) with porcelain ball elephant trunk (7) simultaneously.
6. the low-temperature pyrolysis equipment for low-rank coal, resinous shale, petroleum residue according to claim 1, it is characterized in that: described feeding serew drive-motor (3) and main motor (30) are variable-frequency motor.
One kind adopt claim 1～6 any one described for low-rank coal, resinous shale, the low-temperature cracking process of the low-temperature pyrolysis equipment of petroleum residue, it is characterized in that: material and heated porcelain ball enter material by material elephant trunk (6) and porcelain ball elephant trunk (7) respectively and heat the feeding mouth of porcelain ball mixing auger feeding machine, feeding serew (4) rotates under the drive of feeding serew drive-motor (3), material and hot porcelain ball are mixed and push in the cavity of gas retort revolution main frame, and enter into different pyrolysis reaction region respectively with the rotation of gas retort revolution main frame and divide in the compartment (38), on the cross section of gas retort revolution main frame, store in each pyrolysis reaction region point compartment (38) and go up material and hot porcelain ball, material and hot porcelain ball are along with the abundant hybrid concurrency of revolution of gas retort revolution main frame is given birth to heat exchange, material heats up and pyrolytic reaction takes place, hot porcelain ball is then lowered the temperature chemical reaction is not taken place, carbonizing gas is separated out and is derived backward from the cavity upper space of gas retort revolution main frame, enter at last in the gas solid separation case, material in the pyrolysis reaction region point compartment (38) and porcelain ball under the effect of gravity constantly by moving to low level from a high position, the discharge zone that is pooled to afterbody at last divides in the compartment (39), material and the porcelain ball of having put heat are promoted in the discharging quill shaft (27) to the inverse-arc shape plate of installing (19) by the interior derotation of discharge zone point compartment (39), again in discharging quill shaft (27) enters gas solid separation case body (26), material and soft-paste ball sink down into semicoke and porcelain ball discharging blocking valve (25) in gas solid separation case body (26), semicoke and porcelain ball discharging blocking valve (25) only allow solid materials and porcelain ball to discharge and do not allow carbonizing gas to discharge, and carbonizing gas is discharged by the destructive distillation gas outlet (22) of gas solid separation box top.
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|---|---|---|---|---|
| CN102942940B (en) * | 2012-11-22 | 2013-09-04 | 北京国电龙源环保工程有限公司 | Dual-cone spiral forced feeding device |
| CN104479740B (en) * | 2014-11-26 | 2017-02-01 | 北京贝睿通信息咨询有限公司 | Horizontal high-temperature decomposition and gasification reaction device |
| CN104531195B (en) * | 2014-12-30 | 2016-04-06 | 东北电力大学 | A kind of external-heat oil shale distillation process |
| CN105778943B (en) * | 2016-04-29 | 2019-03-08 | 徐州曹氏化工机械制造有限公司 | A kind of feedstock device for reacting furnace in pyrolysis of coal revolving burner chemical system |
| CN109385286B (en) * | 2017-08-04 | 2021-04-06 | 神华集团有限责任公司 | Continuous pyrolysis device and method suitable for direct coal liquefaction residues |
| CN107892933A (en) * | 2017-11-22 | 2018-04-10 | 洛阳建材建筑设计研究院有限公司 | A kind of heating technique of oil shale swinging gas retort indirect heating apparatus |
| WO2021016877A1 (en) * | 2019-07-30 | 2021-02-04 | 李媛媛 | Material-handling device |
| CN113801668B (en) * | 2021-10-09 | 2022-09-27 | 山东祥桓环境科技有限公司 | Drying and pyrolysis integrated device and process for ball co-heating and crushing |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102329628A (en) * | 2011-08-31 | 2012-01-25 | 华北电力大学（保定） | Large-size low-temperature destructive distillation system for low-order lignite |
| CN102417823A (en) * | 2011-10-21 | 2012-04-18 | 山东天力干燥股份有限公司 | Drying and dry distillation combined quality improving process and system for low rank coal |
| CN202610181U (en) * | 2012-06-08 | 2012-12-19 | 北京国电龙源环保工程有限公司 | Low temperature carbonization device used for low-rank coal and oil shale and oil residue |
-
2012
- 2012-06-08 CN CN 201210187990 patent/CN102757805B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102329628A (en) * | 2011-08-31 | 2012-01-25 | 华北电力大学（保定） | Large-size low-temperature destructive distillation system for low-order lignite |
| CN102417823A (en) * | 2011-10-21 | 2012-04-18 | 山东天力干燥股份有限公司 | Drying and dry distillation combined quality improving process and system for low rank coal |
| CN202610181U (en) * | 2012-06-08 | 2012-12-19 | 北京国电龙源环保工程有限公司 | Low temperature carbonization device used for low-rank coal and oil shale and oil residue |
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