CN103361091A - Solar-energy house refuse low-temperature circulating destructive distillation workshop - Google Patents
Solar-energy house refuse low-temperature circulating destructive distillation workshop Download PDFInfo
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- CN103361091A CN103361091A CN2013103106751A CN201310310675A CN103361091A CN 103361091 A CN103361091 A CN 103361091A CN 2013103106751 A CN2013103106751 A CN 2013103106751A CN 201310310675 A CN201310310675 A CN 201310310675A CN 103361091 A CN103361091 A CN 103361091A
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Abstract
The invention belongs to the house refuse disposal field, particularly belongs to a solar-energy house refuse low-temperature circulating destructive distillation workshop. Information shows that: one person abandons 0.8 kilogram of the house refuse every day, then 800 tons of the house refuse is produced per million persons every day. At present, disposal methods of the house refuse comprise a landfill method, a burning method and the like. But the disposal methods have defects of large land occupation area and high cost of disposal, and even have potential current malpractice of environmental pollution. A solar-energy house refuse destructive distillation method has the advantages of high efficiency, accurate gradation, easiness in classification, less land occupation, no pollution, and change of the waste matters to the useful matters. The method comprises the following technological processes: cleaning and grading, screening and classifying, drying and crushing, granulation and destructive distillation, and sorting and purification. Through use of the solar-energy house refuse destructive distillation method, the organic house refuse after the treatment and granulation is subjected to, in the absence of air, a chemical reaction of heat decomposition, and finally three-state chemical energy products of gas, liquid and solid are obtained, so that the solar-energy house refuse destructive distillation method is breakthrough innovative technology for realization of amount reduction, harmlessness, reclamation of house refuse disposal.
Description
Technical field
The invention belongs to the field of domestic rubbish disposal, especially sun power domestic refuse cold cycle destructive distillation workshop.
Background technology
Domestic refuse is the first-class trouble of standing in the breach in urban health work.Along with the propelling of urbanization state basic policy, urban population is explosive to be increased, and the burden of domestic refuse also rapidly promotes thereupon! How to handle the practical problems that domestic refuse is relatively had a headache to become governments at all levels well, the addressing event of the burning power plant in Fanyu, Guangdong in 2009, caused the condition of the people of seething with excitement, and causes the various places common people's concern.Existing processing domestic refuse method has: the means such as landfill, burning, compost.
The garbage loading embeading method.It is the main method that China's most city solves the domestic refuse outlet.Its shortcoming is, the rubbish of landfill does not carry out harmless treatment, residual a large amount of bacteriums, virus; The hidden danger such as biogas, heavy metal contamination also lie dormant; Its garbage leaching liquid is ground contamination groundwater resource for a long time also, so, this method potential greatly harm, can bring infinite future trouble to the descendants.This method does not only realize the recycling treatment of rubbish, and a large amount of land occupation is that source of pollution are retained to the dangerous way to the descendants.Current many developed countries prohibite landfill waste.
The waste incineration method.According to the research of Zhao senior fellow Zhang Yuan of institute of Research of Environmental Sciences, the waste incineration engineering of China is expansion rapidly.In fact, be not only Beijing, Guangzhou, Nanjing, Suzhou, in China, almost each is economized and is building or preparing to build garbage incinerating power plant.But urban is also arranged, as Kunming etc., take a clear-cut stand not adopt the garbage incineration method treating refuse.Waste incineration has at present caused colony's event and has complained to the higher authorities about an injustice and request fair settlement in a large number and lawsuit.The colony's protest caused as the north of the Changjiang River, Nanjing garbage incinerating power plant project, the protest of mourning in silence on refuse-burning plant doorway, Wujiang, Jiangsu, Bei Jingdong village garbage burning factory contentious case etc.Garbage incineration technology belongs to setting sun technology abroad, and waste incineration is resisted by more developed country.Control the international capital strength of incineration technology and seen this block manure meat of China, the technology transplant China that the means such as attempt utilization bribery are checkmated it, continue its life, expands its capital.
The waste incineration method should be the typical case of pseudoscience.This so-called " environmental protection and energy saving technology " has been the chrysanthemum of yesterday in the world.1985, the U.S. had the plan of the incinerator construction over 137 to be cancelled; 1992, the ban that incinerator uses was passed through in Ontario, Canada; Within 1996, North America has 52 incinerators out of service; The European countries such as German, Dutch, Belgian also promulgate " incinerator is prohibited to build to be made " in succession; 1998, Japan forever closed more than 2000 industrial waste incinerator, and in July, 2000, existing 4600 the waste incineration facilities of Japan are stopped using; Even economy is not the ban that very flourishing Philippines has also promulgated the waste incineration Facilities Construction.2007, former State Environmental Protection Administration required Haidian District Liu Litun waste incineration and generating electricity project to postpone.
The waste incineration method also has many drawbacks, as expensive as cost, complicated operation, if various rubbish mixes, its efficiency can seriously reduce, and latent pollute may be for seriously.What the public worried most is to contain a large amount of organic chlorine-bearing compounds in urban solid garbage, and organic chlorine-bearing compound, comprise, the chemical substances such as sodium-chlor, Repone K in discarded petroleum products, plastic containing chlorine and domestic refuse.Organic chlorine-bearing compound will produce a large amount of Dioxins after burning.
The rubbish dry distillation.Be a kind of new model that adopts dry distillation processing domestic refuse, the domestic refuse dry distillation, comprise, cleans classification, screening sorting, dry pulverizing, granulation destructive distillation and arrange the technical process of purifying.The domestic refuse dry distillation, to choose through cleaning classification, screening sorting, drying the organic constituent after pulverizing, carry out granulation, the organic constituent of granulation is inputted in totally enclosed high temperature carbonization tower and carried out decomposition, generate the chemical energy product of new gas-liquid-solid three-state, so its " resource utilization " degree is close to 100% from theoretical speech, changing waste into valuables, effect is very aobvious different; More due to, destructive distillation is carried out in the granulation of domestic refuse organic constituent in hermetic hot environment, is decomposition reaction completely, so zero release does not have least bit falseness, " innoxious " is also just very clear; The domestic refuse dry distillation, become original trouble maker 100% chemical energy product of newborn gas-liquid-solid three-state, realized the purpose that domestic refuse promotion " resource utilization, innoxious, minimizing " is processed.
Summary of the invention
The present invention's purpose is to disclose the technological line in a kind of sun power domestic refuse cold cycle destructive distillation workshop to society.
The invention belongs to the field of domestic rubbish disposal, particularly sun power domestic refuse cold cycle destructive distillation workshop, provide and show, and can discard per capita 0.8 kilogram of domestic refuse every day, and so, every a population of one million will produce 800 tons of domestic refuses every day! Instantly, life refuse processing method has landfill method, burning method etc.But there is the defect that floor space is large, processing costs is high in these methods, the current social maladies of potentially contaminated environment more.This case sun power domestic refuse dry distillation, have that effect is high, classification is accurate, classification is easy; Take up an area less, the advantage of nuisanceless, waste becoming treasure, its technical process comprises: clean classification, sifting sort, oven dry pulverizing, granulation destructive distillation and arrange and purify.Described sun power domestic refuse dry distillation, by the organic domestic waste after above-mentioned processing granulation, carry out the chemical reaction of thermal degradation under isolated air conditions, the final gas-liquid-solid three-state chemical energy product that generates is to realize the breakthrough innovative technology of " minimizing, innoxious, resource utilization " processing domestic refuse.
The invention has the advantages that.
Energy efficiency is high, and operating cost is low.The present invention adopts real-time follow-up sunlight axle, lens group optically focused, the heat radiation of refrigerant case, refrigerant type sun power cantilever tower to adopt the complex art of energy, two kinds of solar energy converting energy of get both photovoltaic generation and refrigerant heat radiation, and power self-support is self-sustaining, and operation cost reduces naturally.
" resource utilization " degree is high.Domestic refuse is implemented dry distillation " three change " and is processed, carry out decomposition in totally enclosed high temperature carbonization tower, generate the chemical energy product of new gas-liquid-solid three-state, " resource utilization " degree is close to 100% from theoretical speech, changing waste into valuables, effect is fairly obvious.
" innoxious " is very clear.Sun power is generally acknowledged clean energy, the application clean energy, process domestic refuse, due to the domestic refuse of pressing organic constituent classification granulation, carrying out destructive distillation in hermetic hot environment, is decomposition reaction completely, so, zero release does not have least bit falseness, and " innoxious " is also just very clear.Realize genuine domestic refuse " resource utilization, innoxious, minimizing " processing intent.
Technical scheme of the present invention is stated as follows.
Sun power domestic refuse cold cycle destructive distillation workshop, be comprised of two major parts, and the one,, the solar energy source system; The 2nd,, domestic refuse cold cycle destructive distillation workshop.Described solar energy source system is the main source of energy of supplying with the domestic refuse daily operation in cold cycle destructive distillation workshop.
Described solar energy source system, comprise, adopting can system (01), transmission system (02), can adjusting system (03), supervisory system (04), refrigerant type sun power cantilever tower (32), hydraulic power unit (36), straight angle tracker (37), Master Control Room (38), refrigerant type solar panels (40), hang down angle tracking unit (41), refrigerant pumping plant (42), heating agent basin (45), thermal-medium boiler (48), hold, change, power distribution room (49), automatic power switch (50) and national grid (51).
Described domestic refuse cold cycle destructive distillation workshop, comprise: cold cycle dry distillation tower (52), liquid pipe communicating valve (71), water-and-oil separator (72), heating agent pumps into pipe (73), liquid communicating pipe (74), liquid trap (75), solids discharge port (76), solids discharging switch (77), centrifugal and purification process (78), heating agent coil pipe (79), heat medium pipe thermal insulation layer (80), storagetank (81), heat medium pump (82), heating agent return pipe (83), heating agent pumps pipe (84), feeding tube (85), vacuum feeder (86), liquid trap communicating pipe (87), gaseous state collection tube (88), dry distillation tower seat (89), tower under destructive distillation (90), tower in destructive distillation (91), gas, liquid isocon (92), emergency maintenance window (93), condenser (94), and gas holder and valve (95).
The generation of domestic refuse, be not to be subject to artificial to expect and the time limits, so design cold cycle dry distillation tower (52), must be greater than two covers, in order to occurring unpredictable and needing still can guarantee frequent operation in the situation of maintenance.
The diameter of described cold cycle dry distillation tower (52), be advisable to be not more than six meters, the height with lower than 20 meters comparatively suitable, in order to select conventional auxiliary machinery.The single assembly of specification like this, its capacity can reach 500M
3left and right.
The pyrolysis temperature of setting tower (91) in destructive distillation is 350 ℃, 450 ℃ of the temperature of the destructive distillation of tower under destructive distillation (90).
The time of setting low-temperature pyrolysis is twenty four hours.
The keying that setting is positioned at the solids discharging switch (77) of cold cycle dry distillation tower (52) bottom is spaced apart: one hour/time; The material loading operation of described discharging operation and vacuum feeder (86), synchronously carry out.
Above-mentioned setting, the daily handling ability of two covering devices when 800 tons upper and lower, can meet " three change processing " of a population of one million domestic refuse.
Described 1/2 place that is tower cold cycle dry distillation tower (52), be divided into tower (90) under tower in destructive distillation (91) and destructive distillation; Under tower in described destructive distillation (91) and destructive distillation, the bottom of tower (90), all be designed to be 15
.the tapered bottom at angle.
The boundary of tower (90) under tower in described destructive distillation (91) and destructive distillation, be provided with emergency maintenance window (93); Described heating agent pumps pipe (84) and heating agent return pipe (83) all accesses and picks out through emergency maintenance window (93).
The outer wall of described cold cycle dry distillation tower (52), adopt the thermal-insulation heat-resistant shaped material to build by laying bricks or stones; The inwall of cold cycle dry distillation tower (52) adopts stainless steel to make.
Between described outer wall and inwall, be provided with the heat medium pipe thermal insulation layer (80) of coated heating agent coil pipe (79).
The two ends of described heating agent coil pipe (79), the heating agent of one end and heat medium pump (82) pumps pipe (84) and is connected, the other end is connected with heating agent return pipe (83), and the low temperature heating agent after heating imports in the low-temp. portion that heating agent tank (45) is divided into two ones via heating agent return pipe (83).
The top of described cold cycle dry distillation tower (52), be provided with the material loading mouth of pipe, the material loading mouth of pipe and feeding tube (85) are connected, feeding tube (85) is connected with vacuum feeder (86), vacuum feeder (86) sucks the particulate material for the treatment of destructive distillation of organic domestic waste through granulation from storagetank (81), and in input cold cycle dry distillation tower (52).
The upper end of described gaseous state collection tube (88), from the air outlet that is positioned at cold cycle dry distillation tower (52) top, be connected, the below of the lower port access condenser (94) of gaseous state collection tube (88), the carbonization gas of gaseous state is through condenser (94) condensation, isolated inflammable gas also is collected in gas holder, implements next step in-depth and processes.
Described gas, liquid isocon (92), be positioned at the center of cold cycle dry distillation tower (52), connects in destructive distillation tower (90) under tower (91) and destructive distillation.
Described gas, liquid isocon (92), be positioned on the tube wall of tower, is provided with cellular circular hole, in order to gas, liquid, enters in gas, liquid isocon (92), realizes the shunting of gas, liquid destructive distillation product.
Described gas, liquid isocon (92) pass the part at the bottom of tower, are not establish cellular circular hole, with cold cycle dry distillation tower (52), can form sealed structure.
Described gas, liquid isocon (92) pass the port of tower bottom, insertion is arranged in the liquid trap (75) of dry distillation tower seat (89), liquid destructive distillation product in dry distillation tower seat (89) liquid trap (75), seal the port of gas, liquid isocon (92) insertion, form the totally enclosed structure of cold cycle dry distillation tower (52).
The described liquid trap (75) that is arranged in two the dry distillation tower seats in left and right (89), by being connected liquid trap communicating pipe (87), liquefied substance in two liquid traps (75) through connecting, in liquid communicating pipe (74) and liquid pipe communicating valve (71) access water-and-oil separator (72).
The described liquid product that enters different specific weight in water-and-oil separator (72), enter respectively centrifugal and purification process (78) enforcement in-depth processing.
In described dry distillation tower seat (89), also be provided with solids discharge port (76), described solids discharge port (76) is upper, is provided with solids discharging switch (77); Described discharging switch (77), be positioned at the eccentric position be at the bottom of the tapering tower upper, and the solids that destructive distillation produces is discharged via described solids discharge port (76).
Described refrigerant type sun power cantilever tower (32), comprise: right solar panels (106), king-post (35), straight angle tracker (37), pipeline connection box (39), refrigerant type solar panel (40), angle tracking unit (41) hangs down, the curved column base of cantilever (99), end face solar panels (100), swinging strut (101), cryogenic pipe (102), high temperature conduit (103), hydraulicefficiency pipeline (104), electrical pipeline (105), the curved post of cantilever (34), cantilever seat bolt (107), left solar panels (108), pipeline house steward (109), king-post seat (33), bearing A(111), horizontal rotary gear (112), bearing B(113) and worm gear reducer motor (110).
The solar panels of described refrigerant type sun power cantilever tower (32) (100,108,106), be installed on respectively the end face of the king-post (35) that is hollow structure and the curved post of cantilever (34) that layering is arranged at king-post (35) both sides upper, form the structure of sun power cantilever post type.
The width of described end face solar panels (1), consistent with the total width of left and right solar panels (33,108) on the curved column base of L-shaped cantilever (99) that is installed on king-post (35) both sides.
The curved post of described cantilever (34) long-armed, by screw thread in conjunction with being connected with the curved column base of cantilever (99); The curved column base of described cantilever (99), be connected with king-post (35) by cantilever seat bolt (107); The galianconism of the curved post of the described cantilever with connecting bend (34), connect piece bolt (129) by cantilever and be connected with the vertical angle tracking unit (41) of solar panels (100,108,106); Described vertical angle tracking unit (41), by swinging strut (101), is connected with the swinging strut (101) of solar panels (100,108,106); Described refrigerant type sun power cantilever tower (32), have generating and the dual-use function of heat supply concurrently.
Described straight angle tracker (37), comprise, bearing A(111), horizontal rotary gear (112), bearing B(113) and worm gear reducer motor (110).
Described straight angle tracker (37), be installed in the king-post seat (33) of king-post (35) below; Described king-post (35) is through circular position, the below of king-post seat (33), and consolidation ground is overlapping and having: bearing A(111), horizontal rotary gear (112) and bearing B(113); Described bearing A(111) and bearing B(113), be installed on respectively in the bearing support of straight angle tracker (37) upper and lower; Described horizontal rotary gear (112), be positioned at bearing A(111) and bearing B(113) in the middle of king-post (35) on.
Described horizontal rotary gear (112) closes with the gear phase corner be positioned on worm gear reducer motor (110); Described king-post (35), under the driving of straight angle tracker (37), can be done the rotation of level; Above-mentioned solar panels (100,108,106) are hanging down angle tracking unit (41) and being positioned under straight angle tracker (37) coordinated drive of king-post (35) below, the axis that makes solar panels (100,108,106) all the time with sunlight axle keeping parallelism.
Described vertical angle tracking unit (41) comprising: solar panels (100,108,106), solar panels link span (116), link span pulley (117), link span chute (118), hydraulic push rod (119), hydraulicvalve (121), link span piece (120), pipeline outlet (122), hydraulicvalve spacer (123), route profiling (124), cantilever contiguous block (125), steady brace (126), joint bolt (127), stud bolt (128), cantilever connect piece bolt (129).
Described solar panels link span (116), be positioned at the center at solar panels (100,108, the 106) back side; Described solar panels link span (116), be " fourth " word shape structure, and the lower end of " fourth " word shape structure " erecting " is linked together with the upper end of the link span piece (120) that is down " fourth " word shape structure by central shaft; Described solar panels (100,108,106) can be done rectilinear rotation on link span piece (120).
Described solar panels link span (116) first, is provided with link span chute (118); Be provided with link span pulley (117) in described link span chute (118); Described link span pulley (117) is connected with hydraulic push rod (119) front end of hydraulicvalve (121), and the expanding-contracting action of hydraulic push rod (119) drives solar panels (100,108,106) to make vertical translational motion.
The joint portion of described link span piece (120) and cantilever contiguous block (125), be the oblate rod structure matched each other, and on described joint portion, is provided with steady brace (126) and the route profiling (124) of mutual adaptation; The pipeline outlet (122) of described route profiling (124) is positioned at the both sides of link span piece (120).
Described link span piece (120) and cantilever contiguous block (125) are upper, are provided with stud bolt (128), cantilever and connect piece bolt (129) and the corresponding bolt hole of hydraulicvalve spacer bolt; Described hydraulicvalve (121), by hydraulicvalve spacer (123), is installed on the upper position of oblate rod structure one side of link span piece (120).
Described transmission system (02) comprising: pipeline connection box (39), cryogenic pipe (102), high temperature conduit (103), hydraulicefficiency pipeline (104), electrical pipeline (105), pipeline house steward (109).
Described pipeline connection box (39), be arranged in the curved column base of cantilever (99); The two ends of described pipeline connection box (39), be provided with and the interface of described each access tube to the input of answering and output; Described cryogenic pipe (102), high temperature conduit (103), hydraulicefficiency pipeline (104) and electrical pipeline (105), by pipeline house steward (109), are communicated with each functional component of solar energy system (01) and energy adjusting system (03), make each parts Collaboration.
Described energy adjusting system (03), comprise, the refrigerant type sun power cantilever tower (32) in solar energy system (01), heating agent basin (45), thermal-medium boiler (48), hold, change, power distribution room (49), automatic power switch (50), national grid (51).
Described refrigerant type sun power cantilever tower (32), adopted the complex art of real-time follow-up sunlight axle, lens group optically focused, refrigerant type solar panels, not only significantly promotes photovoltaic generation usefulness, the refrigerant that also the got both heat radiation heat energy that obtains.
Describedly hold, change, power distribution room (49), receive the electric energy from refrigerant type sun power cantilever tower (32) photovoltaic generation, carry out electric energy electric power storage, inversion, boost and switch.
Described automatic power switch (50), divide three kinds of situations to state: one, in the self-sustaining situation of electric energy self-supporting of refrigerant type sun power cantilever tower (32) photovoltaic generation, hold, change, power distribution room (49) direct-furnish field internally-powered electricity consumption, store battery is implemented to charging, in order to the normal power supply of refrigerant type sun power cantilever tower (32) while not producing electric energy simultaneously; Two, in the not enough situation of the electric energy self-supporting of refrigerant type sun power cantilever tower (32) photovoltaic generation, hold, automatic power switch (50) action in change, power distribution room (49), switch to national grid (51), by national grid (51) supply power; Three, in the situation that the electric energy self-supporting of refrigerant type sun power cantilever tower (32) photovoltaic generation is had a surplus, by automatic power switch (50), to national grid (51), carry power supply.
Described heating agent basin (45), be the structure that is divided into high-temperature portion and low-temp. portion; Described high-temperature portion, receive, store from refrigerant type sun power cantilever tower (32), by refrigerant medium (143), after photovoltaic cell dispels the heat, being obtained heat; Described low-temp. portion, receive via the low temperature refrigerant medium (143) that dry cold cycle dry distillation tower (52) is implemented to reflux after circulating-heating.
The high-temperature portion of described heating agent basin (45), be provided with electric heater (47), to guarantee the design requirements to cold cycle dry distillation tower (52) heat supply; The shell of described heating agent basin (45), be provided with thermal insulation layer (46).
Described thermal-medium boiler (48), by described heating agent basin (45) heat supply, the steam that thermal-medium boiler (48) produces is implemented the indirect type circulating-heating to the drying room coil pipe (63) between drying vehicle; Implement steam direct heating to the heating basin (11) between cleaning Vehicle.
Described supervisory system (04), by installing known automatic monitoring element in Master Control Room (38) concentratedly, realize microcomputer control to each functional component in field; Described supervisory system (04), object and the project of monitoring are: one, the refrigerant type solar panel (40) in refrigerant type sun power cantilever tower (32), and the monitoring project is: the verticality of power generation and heat supply value, solar panel and sunlight axle, refrigerant work feed back temperature for pressure and heating agent; Two, heating agent basin (45), the monitoring project is: the pressure,volume and temperature situation that height is two ones; Three, thermal-medium boiler (48), the monitoring project is: the intact degree of vapor pressure and gas production rate, thermal-medium boiler (48) security device; Four, hold, change, power distribution room (49), the monitoring project is: power supply automatic switchover, voltage, electric current and power supply hold, change, distribution situation; Five, the operation state in each function workshop.
The accompanying drawing explanation
Accompanying drawing 1 is cold cycle destructive distillation of the present invention workshop process flow diagram.
Accompanying drawing 2 is solar energy source system of the present invention and process relation schematic diagram.
Accompanying drawing 3 is refrigerant type sun power cantilever tower of the present invention (32) structural representation.
Accompanying drawing 4 is vertical angle tracking unit (41) structural representation of the present invention.
Embodiment
Fig. 1 mark title is: cold cycle dry distillation tower (52), liquid pipe communicating valve (71), water-and-oil separator (72), heating agent pumps into pipe (73), liquid communicating pipe (74), liquid trap (75), solids discharge port (76), solids discharging switch (77), centrifugal and purification process (78), heating agent coil pipe (79), heat medium pipe thermal insulation layer (80), storagetank (81), heat medium pump (82), heating agent return pipe (83), heating agent pumps pipe (84), feeding tube (85), vacuum feeder (86), liquid trap communicating pipe (87), gaseous state collection tube (88), dry distillation tower seat (89), tower under destructive distillation (90), tower in destructive distillation (91), gas, liquid isocon (92), emergency maintenance window (93), condenser (94), and gas holder and valve (95).
Part mark title relevant to cold cycle destructive distillation workshop in Fig. 2 is: adopt energy system (01), transmission system (02), energy adjusting system (03), supervisory system (04), steam pipeline (31), refrigerant type sun power cantilever tower (32), king-post seat (33), the curved post of cantilever (34), king-post (35), hydraulic power unit (36), straight angle tracker (37), Master Control Room (38), pipeline connection box (39), refrigerant type solar panels (40), angle tracking unit (41) hangs down, refrigerant pumping plant (42), category filter workshop (43), dry and pulverize workshop (44), heating agent basin (45), thermal insulation layer (46), electric heater (47), thermal-medium boiler (48), hold, become, power distribution room (49), automatic power switch (50), national grid (51) and circulation destructive distillation workshop (52).
Fig. 3 mark title is: king-post seat (33), the curved post of cantilever (34), king-post (35), straight angle tracker (37), pipeline connection box (39), refrigerant type solar panels (40), angle tracking unit (41) hangs down, the curved column base of cantilever (99), end face solar panels (100), swinging strut (101), cryogenic pipe (102), high temperature conduit (103), hydraulicefficiency pipeline (104), electrical pipeline (105), right solar panels (106), cantilever seat bolt (107), left solar panels energy (108), pipeline house steward (109), worm gear reducer motor (110), bearing A(111), horizontal rotary gear (112), bearing B(113).
Fig. 4 mark title is: refrigerant type solar panels (40), solar panels link span (116), link span pulley (117), link span chute (118), hydraulic push rod (119), hydraulicvalve (121), link span piece (120), pipeline outlet (122), hydraulicvalve spacer (123), route profiling (124), cantilever contiguous block (125), steady brace (126), joint bolt (127), stud bolt (128), cantilever connect piece bolt (129).
Describe the present invention in detail below in conjunction with accompanying drawing.
As shown in Figure 1, sun power domestic refuse cold cycle destructive distillation workshop, be comprised of two major parts, and the one,, the solar energy source system; The 2nd,, domestic refuse cold cycle destructive distillation workshop.Described solar energy source system is the main source of energy of supplying with the domestic refuse daily operation in cold cycle destructive distillation workshop.
As shown in Figure 1, described solar energy source system, comprise, adopting can system (01), transmission system (02), can adjusting system (03), supervisory system (04), refrigerant type sun power cantilever tower (32), hydraulic power unit (36), straight angle tracker (37), Master Control Room (38), refrigerant type solar panels (40), hang down angle tracking unit (41), refrigerant pumping plant (42), heating agent basin (45), thermal-medium boiler (48), hold, change, power distribution room (49), automatic power switch (50) and national grid (51).
As shown in Figure 1, described domestic refuse cold cycle destructive distillation workshop, comprise: cold cycle dry distillation tower (52), liquid pipe communicating valve (71), water-and-oil separator (72), heating agent pumps into pipe (73), liquid communicating pipe (74), liquid trap (75), solids discharge port (76), solids discharging switch (77), centrifugal and purification process (78), heating agent coil pipe (79), heat medium pipe thermal insulation layer (80), storagetank (81), heat medium pump (82), heating agent return pipe (83), heating agent pumps pipe (84), feeding tube (85), vacuum feeder (86), liquid trap communicating pipe (87), gaseous state collection tube (88), dry distillation tower seat (89), tower under destructive distillation (90), tower in destructive distillation (91), gas, liquid isocon (92), emergency maintenance window (93), condenser (94), and gas holder and valve (95),
The generation of domestic refuse, be not to be subject to artificial to expect and the time limits, so design cold cycle dry distillation tower (52), must be greater than two covers, in order to occurring unpredictable and needing still can guarantee frequent operation in the situation of maintenance.
As shown in Figure 1, the diameter of described cold cycle dry distillation tower (52), be advisable to be not more than six meters, the height with lower than 20 meters comparatively suitable, in order to select conventional auxiliary machinery.The single assembly of specification like this, its capacity can reach 500M
3left and right.
Further, the pyrolysis temperature of setting tower (91) in destructive distillation is 350 ℃, 450 ℃ of the temperature of the destructive distillation of tower under destructive distillation (90).
Further, the time of setting low-temperature pyrolysis is twenty four hours.
Further, the keying of setting the solids discharging switch (77) be positioned at cold cycle dry distillation tower (52) bottom is spaced apart: one hour/time; The material loading operation of described discharging operation and vacuum feeder (86), synchronously carry out.
Above-mentioned setting, the daily handling ability of two covering devices when 800 tons upper and lower, " minimizing, innoxious, the resource utilization " that can meet a population of one million domestic refuse processed.
As shown in Figure 1, described 1/2 place that is tower cold cycle dry distillation tower (52), be divided into tower (90) under tower in destructive distillation (91) and destructive distillation; Under tower in described destructive distillation (91) and destructive distillation, the bottom of tower (90), all be designed to be 15
.the tapered bottom at angle.
As shown in Figure 1, the boundary of tower (90) under tower in described destructive distillation (91) and destructive distillation, be provided with emergency maintenance window (93); Described heating agent pumps pipe (84) and heating agent return pipe (83) all accesses and picks out through emergency maintenance window (93).
As shown in Figure 1, the outer wall of described cold cycle dry distillation tower (52), adopt the thermal-insulation heat-resistant shaped material to build by laying bricks or stones; The inwall of cold cycle dry distillation tower (52) adopts stainless steel to make.
As shown in Figure 1, between described outer wall and inwall, be provided with the heat medium pipe thermal insulation layer (80) of coated heating agent coil pipe (79).
As shown in Figure 1, the two ends of described heating agent coil pipe (79), the heating agent of one end and heat medium pump (82) pumps pipe (84) and is connected, the other end is connected with heating agent return pipe (83), low temperature heating agent after heating, import in the low-temp. portion that heating agent tank (45) is divided into two ones via heating agent return pipe (83).
As shown in Figure 1, the top of described cold cycle dry distillation tower (52), be provided with the material loading mouth of pipe, the material loading mouth of pipe and feeding tube (85) are connected, feeding tube (85) is connected with vacuum feeder (86), vacuum feeder (86) sucks the particulate material for the treatment of destructive distillation of organic domestic waste through granulation from storagetank (81), and in input cold cycle dry distillation tower (52).
As shown in Figure 1, the upper end of described gaseous state collection tube (88), from the air outlet that is positioned at cold cycle dry distillation tower (52) top, be connected, the below of the lower port access condenser (94) of gaseous state collection tube (88), the carbonization gas of gaseous state is through condenser (94) condensation, isolated inflammable gas also is collected in gas holder, implements next step in-depth and processes.
As shown in Figure 1, described gas, liquid isocon (92), be positioned at the center of cold cycle dry distillation tower (52), connects in destructive distillation tower (90) under tower (91) and destructive distillation.
As shown in Figure 1, described gas, liquid isocon (92), be positioned on the tube wall of tower, is provided with cellular circular hole, in order to gas, liquid, enters in gas, liquid isocon (92), realizes the shunting of gas, liquid destructive distillation product.
As shown in Figure 1, described gas, liquid isocon (92) pass the part at the bottom of tower, are not establish cellular circular hole, with cold cycle dry distillation tower (52), can form sealed structure.
As shown in Figure 1, described gas, liquid isocon (92) pass the port of tower bottom, insertion is arranged in the liquid trap (75) of dry distillation tower seat (89), liquid destructive distillation product in dry distillation tower seat (89) liquid trap (75), seal the port of gas, liquid isocon (92) insertion, form the totally enclosed structure of cold cycle dry distillation tower (52).
As shown in Figure 1, the described liquid trap (75) that is arranged in two the dry distillation tower seats in left and right (89), by being connected liquid trap communicating pipe (87), liquefied substance in two liquid traps (75) through connecting, in liquid communicating pipe (74) and liquid pipe communicating valve (71) access water-and-oil separator (72).
As shown in Figure 1, the described liquid product that enters different specific weight in water-and-oil separator (72), enter respectively centrifugal and purification process (78) enforcement in-depth processing.
As shown in Figure 1, in described dry distillation tower seat (89), also be provided with solids discharge port (76), described solids discharge port (76) is upper, is provided with solids discharging switch (77); Described discharging switch (77), be positioned at the eccentric position be at the bottom of the tapering tower upper, and the solids that destructive distillation produces is discharged via described solids discharge port (76).
As shown in Figure 2, described solar energy source system, comprise, adopt energy system (01), transmission system (02), energy adjusting system (03), supervisory system (04), steam pipeline (31), refrigerant type sun power cantilever tower (32), king-post seat (33), the curved post of cantilever (34), king-post (35), hydraulic power unit (36), straight angle tracker (37), Master Control Room (38), pipeline connection box (39), refrigerant type solar panels (40), angle tracking unit (41) hangs down, refrigerant pumping plant (42), heating agent basin (45), thermal insulation layer (46), electric heater (47), thermal-medium boiler (48), hold, become, power distribution room (49), automatic power switch (50) and national grid (51).
As shown in Fig. 2 Fig. 3 Fig. 4, described refrigerant type sun power cantilever tower (32), comprise: king-post seat (33), the curved post of cantilever (34), king-post (35), straight angle tracker (37), pipeline connection box (39), refrigerant type solar panel (40), angle tracking unit (41) hangs down, the curved column base of cantilever (99), end face solar panels (100), swinging strut (101), cryogenic pipe (102), high temperature conduit (103), hydraulicefficiency pipeline (104), electrical pipeline (105), right solar panels (106), cantilever seat bolt (107), left solar panels (108), pipeline house steward (109), bearing A(111), horizontal rotary gear (112), bearing B(113) and worm gear reducer motor (110).
As shown in Figure 2 and Figure 3, the solar panels of described refrigerant type sun power cantilever tower (32) (100,108,106), be installed on respectively the end face of the king-post (35) that is hollow structure and the curved post of cantilever (34) that layering is arranged at king-post (35) both sides upper, form the structure of sun power cantilever post type.
As shown in Figure 2 and Figure 3, the width of described end face solar panels (100), consistent with the total width of left and right solar panels (33,108) on the curved column base of L-shaped cantilever (99) that is installed on king-post (35) both sides.
Shown in Fig. 2, Fig. 3, the curved post of described cantilever (34) long-armed, by screw thread in conjunction with being connected with the curved column base of cantilever (99); The curved column base of described cantilever (99), be connected with king-post (35) by cantilever seat bolt (107).
As shown in Figure 3, the galianconism of the curved post of the described cantilever with connecting bend (34), connect piece bolt (129) by cantilever and be connected with the vertical angle tracking unit (41) of solar panels (100,108,106).
As shown in Figure 3, described vertical angle tracking unit (41), by swinging strut (101), is connected with the swinging strut (101) of solar panels (100,108,106).
As shown in Figure 2, Figure 3, Figure 4, described refrigerant type sun power cantilever tower (32), adopted the complex art of real-time follow-up sunlight axle, lens group optically focused, refrigerant type solar panels, not only significantly promoted photovoltaic generation usefulness, the refrigerant that also the got both heat radiation heat energy that obtains.
As shown in Figure 2, Figure 3, Figure 4, described straight angle tracker (37), comprise, bearing A(111), horizontal rotary gear (112), bearing B(113) and worm gear reducer motor (110).
As shown in Figure 2, Figure 3, Figure 4, described straight angle tracker (37), be installed in the king-post seat (33) of king-post (35) below, described king-post (35) is through circular position, the below of king-post seat (33), and consolidation ground is overlapping and having: bearing A(111), horizontal rotary gear (112) and bearing B(113); Described bearing A(111) and bearing B(113), be installed on respectively in the bearing support of straight angle tracker (37) upper and lower; Described horizontal rotary gear (112), be positioned at bearing A(111) and bearing B(113) in the middle of king-post (35) on; Described horizontal rotary gear (112) closes with the gear phase corner be positioned on worm gear reducer motor (110); Described king-post (35), under the driving of straight angle tracker (37), can be done the rotation of level.
As shown in Fig. 3 Fig. 4, described vertical angle tracking unit (41) comprising: refrigerant type solar panels (40), solar panels link span (116), link span pulley (117), link span chute (118), hydraulic push rod (119), hydraulicvalve (121), link span piece (120), pipeline outlet (122), hydraulicvalve spacer (123), route profiling (124), cantilever contiguous block (125), steady brace (126), joint bolt (127), stud bolt (128), cantilever connect piece bolt (129).
As shown in Figure 4, described solar panels link span (116), be positioned at the center at solar panels (100,108, the 106) back side, be " fourth " word shape structure, the lower end of " fourth " word shape structure " erecting ", linked together with the upper end of the link span piece (120) that is down " fourth " word shape structure by central shaft.
As shown in Figure 4, described refrigerant type solar panels (100,108,106) can be done rectilinear rotation on link span piece (120).
As shown in Figure 4, described solar panels link span (116) first, is provided with link span chute (118).
As shown in Figure 4, be provided with link span pulley (117) in described link span chute (118); Described link span pulley (117) is connected with hydraulic push rod (119) front end of hydraulicvalve (121), and the expanding-contracting action of hydraulic push rod (119) drives solar panels (100,108,106) to make vertical translational motion.
As shown in Figure 4, the joint portion of described link span piece (120) and cantilever contiguous block (125), be the oblate rod structure matched each other.
As shown in Figure 4, on described joint portion, be provided with steady brace (126) and the route profiling (124) of mutual adaptation; The pipeline outlet (122) of described route profiling (124) is positioned at the both sides of link span piece (120);
As shown in Figure 4, described link span piece (120) and cantilever contiguous block (125) are upper, are provided with stud bolt (128), cantilever and connect piece bolt (129) and the corresponding bolt hole of hydraulicvalve spacer bolt.
As shown in Figure 4, described hydraulicvalve (121), by hydraulicvalve spacer (123), is installed on the upper position of oblate rod structure one side of link span piece (120).
As shown in Figure 2, Figure 3, Figure 4, above-mentioned solar panels (100,108,106) are hanging down angle tracking unit (41) and being positioned under straight angle tracker (37) coordinated drive of king-post (35) below, the axis that makes solar panels (100,108,106) all the time with sunlight axle keeping parallelism.
As shown in Figure 2, described transmission system (02) comprising: pipeline connection box (39), cryogenic pipe (102), high temperature conduit (103), hydraulicefficiency pipeline (104), electrical pipeline (105), pipeline house steward (109).
As shown in Figure 2, described pipeline connection box (39), be arranged in the curved column base of cantilever (99); The two ends of described pipeline connection box (39), be provided with and the interface of described each access tube to the input of answering and output.
As shown in Figure 2, described cryogenic pipe (102), high temperature conduit (103), hydraulicefficiency pipeline (104) and electrical pipeline (105) are by pipeline house steward (109), be communicated with each functional component of solar energy system (01) and energy adjusting system (03), make each parts Collaboration.
As shown in Figure 2, describedly hold, change, power distribution room (49), receive the electric energy from refrigerant type sun power cantilever tower (32) photovoltaic generation, carry out electric energy electric power storage, inversion, boost and switch; Described automatic power switch (50), minute three kinds of situations are stated.
One, in the self-sustaining situation of electric energy self-supporting of refrigerant type sun power cantilever tower (32) photovoltaic generation, hold, change, power distribution room (49) direct-furnish field internally-powered electricity consumption, store battery is implemented to charging, in order to the normal power supply of refrigerant type sun power cantilever tower (32) while not producing electric energy simultaneously.
Two, in the not enough situation of the electric energy self-supporting of refrigerant type sun power cantilever tower (32) photovoltaic generation, hold, automatic power switch (50) action in change, power distribution room (49), switch to national grid (51), by national grid (51) supply power.
Three, in the situation that the electric energy self-supporting of refrigerant type sun power cantilever tower (32) photovoltaic generation is had a surplus, by automatic power switch (50), to national grid (51), carry power supply.
As shown in Figure 1, described heating agent basin (45), be the structure that is divided into high-temperature portion and low-temp. portion; Described high-temperature portion, receive, store from refrigerant type sun power cantilever tower (32), by refrigerant medium (143), after photovoltaic cell dispels the heat, being obtained heat.
As shown in Figure 1, described low-temp. portion, receive via the low temperature refrigerant medium (143) that dry cold cycle dry distillation tower (52) is implemented to reflux after circulating-heating.
As shown in Figure 1, the high-temperature portion of described heating agent basin (45), be provided with electric heater (47), to guarantee the design requirements to cold cycle dry distillation tower (52) heat supply.
As shown in Figure 1, the shell of described heating agent basin (45), be provided with thermal insulation layer (46); Described thermal-medium boiler (48), by described heating agent basin (45) heat supply, the steam that thermal-medium boiler (48) produces is implemented the indirect type circulating-heating to the drying room coil pipe (63) between drying vehicle; Implement steam direct heating to the heating basin (11) between cleaning Vehicle.
As shown in Figure 3, described refrigerant type sun power cantilever tower (32), have generating and the dual-use function of heat supply concurrently.
Described supervisory system (04), by installing known automatic monitoring element in Master Control Room (38) concentratedly, realize microcomputer control to each functional component in field.Described supervisory system (04), object and the project of monitoring are: one, the refrigerant type solar panel (40) in refrigerant type sun power cantilever tower (32), and the monitoring project is: the verticality of power generation and heat supply value, solar panel and sunlight axle, refrigerant work feed back temperature for pressure and heating agent; Two, heating agent basin (45), the monitoring project is: the pressure,volume and temperature situation that height is two ones; Three, thermal-medium boiler (48), the monitoring project is: the intact degree of vapor pressure and gas production rate, thermal-medium boiler (48) security device; Four, hold, change, power distribution room (49), the monitoring project is: power supply automatic switchover, voltage, electric current and power supply hold, change, distribution situation; Five, the operation state in each function workshop.
Claims (7)
1. sun power domestic refuse cold cycle destructive distillation workshop, be comprised of two major parts, and the one,, the solar energy source system, the 2nd,, domestic refuse cold cycle destructive distillation workshop, described solar energy source system is the main source of energy of supplying with the domestic refuse daily operation in cold cycle destructive distillation workshop, described solar energy source system, comprise, adopting can system (01), transmission system (02), can adjusting system (03), supervisory system (04), refrigerant type sun power cantilever tower (32), hydraulic power unit (36), straight angle tracker (37), Master Control Room (38), refrigerant type solar panels (40), hang down angle tracking unit (41), refrigerant pumping plant (42), heating agent basin (45), thermal-medium boiler (48), hold, change, power distribution room (49), automatic power switch (50) and national grid (51), described domestic refuse cold cycle destructive distillation workshop, comprise: cold cycle dry distillation tower (52), liquid pipe communicating valve (71), water-and-oil separator (72), heating agent pumps into pipe (73), liquid communicating pipe (74), liquid trap (75), solids discharge port (76), solids discharging switch (77), centrifugal and purification process (78), heating agent coil pipe (79), heat medium pipe thermal insulation layer (80), storagetank (81), heat medium pump (82), heating agent return pipe (83), heating agent pumps pipe (84), feeding tube (85), vacuum feeder (86), liquid trap communicating pipe (87), gaseous state collection tube (88), dry distillation tower seat (89), tower under destructive distillation (90), tower in destructive distillation (91), gas, liquid isocon (92), emergency maintenance window (93), condenser (94), and gas holder and valve (95), domestic refuse, all producing, be not limited by people's wish and time all the time, so, when design or installation cold cycle dry distillation tower (52), must be greater than 1+X, to ensure in imprevision and maintenance situation, still can often run, it is characterized in that: the diameter of described cold cycle dry distillation tower (52), to be not more than six meters, be advisable, the height with lower than 20 meters comparatively suitable, in order to select conventional auxiliary machinery, the capacity of this specification can reach 500M
3, the pyrolysis temperature of setting tower (91) in destructive distillation is 300 ℃, 400 ℃ of the temperature of the destructive distillation of tower under destructive distillation (90), setting pyrolyzate is twenty four hours in the dry distillation tower residence time, the keying of setting solids discharging switch (77) is spaced apart: one hour/time, set discharging operation and material loading operation, synchronous same amount is carried out, above-mentioned setting, the daily handling ability of two covering devices when 800 tons upper and lower, can meet a population of one million domestic refuse and realize that " minimizing, innoxious, resource utilization " process, described cold cycle dry distillation tower (52), tower, 1/2 place of tower, be divided into tower (90) under tower in destructive distillation (91) and destructive distillation, under tower in described destructive distillation (91) and destructive distillation, the bottom of tower (90), all be designed to be 15
.the tapered bottom at angle, the boundary of tower (90) under tower in described destructive distillation (91) and destructive distillation, be provided with emergency maintenance window (93), described heating agent pumps pipe (84) and heating agent return pipe (83) all accesses and picks out through emergency maintenance window (93), the outer wall of described cold cycle dry distillation tower (52), adopt the thermal-insulation heat-resistant shaped material to build by laying bricks or stones, the inwall of cold cycle dry distillation tower (52) adopts stainless steel to make, between described outer wall and inwall, be provided with the heat medium pipe thermal insulation layer (80) of coated heating agent coil pipe (79), the two ends of described heating agent coil pipe (79), the heating agent of one end and heat medium pump (82) pumps pipe (84) and is connected, the other end is connected with heating agent return pipe (83), and the low temperature heating agent after heating imports in the low-temp. portion that heating agent tank (45) is divided into two ones via heating agent return pipe (83), the top of described cold cycle dry distillation tower (52), be provided with the material loading mouth of pipe, the material loading mouth of pipe and feeding tube (85) are connected, feeding tube (85) is connected with vacuum feeder (86), vacuum feeder (86) sucks the particulate material for the treatment of destructive distillation of organic domestic waste through granulation from storagetank (81), and in input cold cycle dry distillation tower (52), the upper end of described gaseous state collection tube (88), from the air outlet that is positioned at cold cycle dry distillation tower (52) top, be connected, the below of the lower port access condenser (94) of gaseous state collection tube (88), the carbonization gas of gaseous state is through condenser (94) condensation, isolated inflammable gas also is collected in gas holder, implements next step in-depth and processes, described gas, liquid isocon (92), be positioned at the center of cold cycle dry distillation tower (52), connects in destructive distillation tower (90) under tower (91) and destructive distillation, described gas, liquid isocon (92), be positioned on the tube wall of tower, is provided with cellular circular hole, in order to gas, liquid, enters in gas, liquid isocon (92), realizes the shunting of gas, liquid destructive distillation product, described gas, liquid isocon (92) pass the part at the bottom of tower, are not establish cellular circular hole, with cold cycle dry distillation tower (52), can form sealed structure, described gas, liquid isocon (92) pass the port of tower bottom, insertion is arranged in the liquid trap (75) of dry distillation tower seat (89), liquid destructive distillation product in dry distillation tower seat (89) liquid trap (75), seal the port of gas, liquid isocon (92) insertion, form the totally enclosed structure of cold cycle dry distillation tower (52), the described liquid trap (75) that is arranged in two the dry distillation tower seats in left and right (89), by being connected liquid trap communicating pipe (87), liquefied substance in two liquid traps (75) through connecting, in liquid communicating pipe (74) and liquid pipe communicating valve (71) access water-and-oil separator (72), the described liquid product that enters different specific weight in water-and-oil separator (72), enter respectively centrifugal and purification process (78) enforcement in-depth processing, in described dry distillation tower seat (89), also be provided with solids discharge port (76), described solids discharge port (76) is upper, is provided with solids discharging switch (77), described discharging switch (77), be positioned at the eccentric position be at the bottom of the tapering tower upper, and the solids that destructive distillation produces is discharged via described solids discharge port (76).
2. sun power domestic refuse cold cycle destructive distillation according to claim 1 workshop, it is characterized in that, described refrigerant type sun power cantilever tower (32), comprise: king-post (35), straight angle tracker (37), pipeline connection box (39), refrigerant type solar panel (40), angle tracking unit (41) hangs down, right solar panels (106), the curved column base of cantilever (99), end face solar panels (100), swinging strut (101), cryogenic pipe (102), high temperature conduit (103), hydraulicefficiency pipeline (104), electrical pipeline (105), the curved post of cantilever (34), cantilever seat bolt (107), left solar panels (108), pipeline house steward (109), king-post seat (33), bearing A(111), horizontal rotary gear (112), bearing B(113) and worm gear reducer motor (110), the solar panels of described refrigerant type sun power cantilever tower (32) (100,108,106), be installed on respectively the end face of the king-post (35) that is hollow structure and the curved post of cantilever (34) that layering is arranged at king-post (35) both sides upper, form the structure of sun power cantilever post type, the width of described end face solar panels (100), consistent with the total width of left and right solar panels (108,106) on the curved column base of L-shaped cantilever (99) that is installed on king-post (35) both sides, the curved post of described cantilever (34) long-armed, by screw thread in conjunction with being connected with the curved column base of cantilever (99), the curved column base of described cantilever (99), be connected with king-post (35) by cantilever seat bolt (107), the galianconism of the curved post of the described cantilever with connecting bend (34), connect piece bolt (129) by cantilever and be connected with the vertical angle tracking unit (41) of solar panels (100,108,106), described vertical angle tracking unit (41), by swinging strut (101), is connected with the swinging strut (101) of solar panels (100,108,106), described refrigerant type sun power cantilever tower (32), have generating and the dual-use function of heat supply concurrently.
3. sun power domestic refuse cold cycle destructive distillation according to claim 1 workshop, it is characterized in that, described straight angle tracker (37), comprise, bearing A(111), horizontal rotary gear (112), bearing B(113) and worm gear reducer motor (110); Described straight angle tracker (37), be installed in the king-post seat (33) of king-post (35) below, described king-post (35) is through circular position, the below of king-post seat (33), and consolidation ground is overlapping and having: bearing A(111), horizontal rotary gear (112) and bearing B(113); Described bearing A(111) and bearing B(113), be installed on respectively in the bearing support of straight angle tracker (37) upper and lower; Described horizontal rotary gear (112), be positioned at bearing A(111) and bearing B(113) in the middle of king-post (35) on; Described horizontal rotary gear (112) closes with the gear phase corner be positioned on worm gear reducer motor (110); Described king-post (35), under the driving of straight angle tracker (37), can be done the rotation of level; Above-mentioned solar panels (100,108,106) are hanging down angle tracking unit (41) and being positioned under straight angle tracker (37) coordinated drive of king-post (35) below, the axis that makes solar panels (100,108,106) all the time with sunlight axle keeping parallelism.
4. sun power domestic refuse cold cycle destructive distillation according to claim 1 workshop, it is characterized in that, described vertical angle tracking unit (41), comprise: solar panels (100, 108, 106), solar panels link span (116), link span pulley (117), link span chute (118), hydraulic push rod (119), hydraulicvalve (121), link span piece (120), pipeline outlet (122), hydraulicvalve spacer (123), route profiling (124), cantilever contiguous block (125), steady brace (126), joint bolt (127), stud bolt (128), cantilever connects piece bolt (129), described solar panels link span (116), be positioned at the center at solar panels (100,108, the 106) back side, described solar panels link span (116), be " fourth " word shape structure, and the lower end of " fourth " word shape structure " erecting " is linked together with the upper end of the link span piece (120) that is down " fourth " word shape structure by central shaft, described solar panels (100,108,106) can be done rectilinear rotation on link span piece (120), described solar panels link span (116) first, is provided with link span chute (118), be provided with link span pulley (117) in described link span chute (118), described link span pulley (117) is connected with hydraulic push rod (119) front end of hydraulicvalve (121), and the expanding-contracting action of hydraulic push rod (119) drives solar panels (100,108,106) to make vertical translational motion, the joint portion of described link span piece (120) and cantilever contiguous block (125), be the oblate rod structure matched each other, and on described joint portion, is provided with steady brace (126) and the route profiling (124) of mutual adaptation, the pipeline outlet (122) of described route profiling (124) is positioned at the both sides of link span piece (120), described link span piece (120) and cantilever contiguous block (125) are upper, are provided with stud bolt (128), cantilever and connect piece bolt (129) and the corresponding bolt hole of hydraulicvalve spacer bolt, described hydraulicvalve (121), by hydraulicvalve spacer (123), is installed on the upper position of oblate rod structure one side of link span piece (120).
5. sun power domestic refuse cold cycle destructive distillation according to claim 1 workshop, it is characterized in that, described transmission system (02) comprising: pipeline connection box (39), cryogenic pipe (102), high temperature conduit (103), hydraulicefficiency pipeline (104), electrical pipeline (105), pipeline house steward (109); Described pipeline connection box (39), be arranged in the curved column base of cantilever (99); The two ends of described pipeline connection box (39), be provided with and the interface of described each access tube to the input of answering and output; Described cryogenic pipe (102), high temperature conduit (103), hydraulicefficiency pipeline (104) and electrical pipeline (105), by pipeline house steward (109), are communicated with each functional component of solar energy system (01) and energy adjusting system (03), make each parts Collaboration.
6. sun power domestic refuse cold cycle destructive distillation according to claim 1 workshop, it is characterized in that, described energy adjusting system (03), comprise, the refrigerant type sun power cantilever tower (32) in solar energy system (01), heating agent basin (45), thermal-medium boiler (48), hold, change, power distribution room (49), automatic power switch (50), national grid (51), refrigerant medium (143) and refrigerant case (144); Described refrigerant type sun power cantilever tower (32), adopted the complex art of real-time follow-up sunlight axle, lens group optically focused, refrigerant type solar panels, not only significantly promotes photovoltaic generation usefulness, the refrigerant that also the got both heat radiation heat energy that obtains; Describedly hold, change, power distribution room (49), receive the electric energy from refrigerant type sun power cantilever tower (32) photovoltaic generation, carry out electric energy electric power storage, inversion, boost and switch; Described automatic power switch (50), divide three kinds of situations to state: one, in the self-sustaining situation of electric energy self-supporting of refrigerant type sun power cantilever tower (32) photovoltaic generation, hold, change, power distribution room (49) direct-furnish field internally-powered electricity consumption, store battery is implemented to charging, in order to the normal power supply of refrigerant type sun power cantilever tower (32) while not producing electric energy simultaneously; Two, in the not enough situation of the electric energy self-supporting of refrigerant type sun power cantilever tower (32) photovoltaic generation, hold, automatic power switch (50) action in change, power distribution room (49), switch to national grid (51), by national grid (51) supply power; Three, in the situation that the electric energy self-supporting of refrigerant type sun power cantilever tower (32) photovoltaic generation is had a surplus, by automatic power switch (50), to national grid (51), carry power supply; Described heating agent basin (45), be the structure that is divided into high-temperature portion and low-temp. portion; Described high-temperature portion, receive, store from refrigerant type sun power cantilever tower (32), by refrigerant medium (143), after photovoltaic cell dispels the heat, being obtained heat; Described low-temp. portion, receive via the low temperature refrigerant medium (143) that dry cold cycle dry distillation tower (52) is implemented to reflux after circulating-heating; The high-temperature portion of described heating agent basin (45), be provided with electric heater (47), to guarantee the design requirements to cold cycle dry distillation tower (52) heat supply; The shell of described heating agent basin (45), be provided with thermal insulation layer (46); Described thermal-medium boiler (48), by described heating agent basin (45) heat supply, the steam that thermal-medium boiler (48) produces is implemented the indirect type circulating-heating to the drying room coil pipe (63) between drying vehicle; Implement steam direct heating to the heating basin (11) between cleaning Vehicle.
7. sun power domestic refuse cold cycle destructive distillation according to claim 1 workshop, it is characterized in that, described supervisory system (04), by installing known automatic monitoring element in Master Control Room (38) concentratedly, each functional component in field is realized to microcomputer control, the object of its monitoring and project are: one, the refrigerant type solar panel (40) in refrigerant type sun power cantilever tower (32), and the monitoring project is: the verticality of power generation and heat supply value, solar panel and sunlight axle, refrigerant work feed back temperature for pressure and heating agent; Two, heating agent basin (45), the monitoring project is: the pressure,volume and temperature situation that height is two ones; Three, thermal-medium boiler (48), the monitoring project is: the intact degree of vapor pressure and gas production rate, thermal-medium boiler (48) security device; Four, hold, change, power distribution room (49), the monitoring project is: power supply automatic switchover, voltage, electric current and power supply hold, change, distribution situation; Five, the operation state in each function workshop.
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| CN201310310675.1A CN103361091B (en) | 2013-07-24 | 2013-07-24 | Solar-energy house refuse low-temperature circulating destructive distillation workshop |
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| CN201310310675.1A CN103361091B (en) | 2013-07-24 | 2013-07-24 | Solar-energy house refuse low-temperature circulating destructive distillation workshop |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4382850A (en) * | 1981-04-28 | 1983-05-10 | The United States Of America As Represented By The United States Department Of Energy | Solar retorting of oil shale |
| JP2005060589A (en) * | 2003-08-18 | 2005-03-10 | Tsuruhiko Kiuchi | Waste carbonization system |
| CN2932222Y (en) * | 2006-07-25 | 2007-08-08 | 徐铁良 | Dry distillation device of solar furnace |
| CN203039617U (en) * | 2012-12-31 | 2013-07-03 | 李万红 | Solar-energy cantilever-tower-pillar-type thermal-arrest energy-conversion thermal power station |
| CN203346336U (en) * | 2013-07-24 | 2013-12-18 | 李万红 | Solar domestic garbage low-temperature circular dry distillation workshop |
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