CN1656340A - High performance heat storage high temperature system for decomposition of effluent and organic garbage - Google Patents

High performance heat storage high temperature system for decomposition of effluent and organic garbage Download PDF

Info

Publication number
CN1656340A
CN1656340A CN03812273.1A CN03812273A CN1656340A CN 1656340 A CN1656340 A CN 1656340A CN 03812273 A CN03812273 A CN 03812273A CN 1656340 A CN1656340 A CN 1656340A
Authority
CN
China
Prior art keywords
heat
hole
tank body
sewage
heat exchange
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN03812273.1A
Other languages
Chinese (zh)
Other versions
CN1318802C (en
Inventor
林茂森
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Publication of CN1656340A publication Critical patent/CN1656340A/en
Application granted granted Critical
Publication of CN1318802C publication Critical patent/CN1318802C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44—Details; Accessories
    • F23G5/46—Recuperation of heat
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/001—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals for sludges or waste products from water treatment installations
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2206/00—Waste heat recuperation
    • F23G2206/20—Waste heat recuperation using the heat in association with another installation
    • F23G2206/203—Waste heat recuperation using the heat in association with another installation with a power/heat generating installation
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/12—Heat utilisation in combustion or incineration of waste

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Processing Of Solid Wastes (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

The present invention relates to a sort of system which can store heat and crack the sewage and organic garbage, it is composed of the highly effective heat-stored pyrolysis sewage which is treated with heat insulation by thermal insulation paint, organic garbage can, heat exchange can, closed-cycle steam turbine, isobaric potential-different water injection arrangement and pipeline; when this system is started, it consumes the energy for only one time, when it works it pyrolyzes the sewage and organic garbage with low consumption of energy and outputs the heat energy to the outside, this equipment have the advantages which includes: low cost, safe operation, no noise, no vibration, no flame, easy operation and the like, and can pyrolyze the sewage and organic garbage with low consumption of energy and can output the electric power and heat energy to the outside.

Description

High performance heat storage high temperature system for decomposition of effluent and organic garbage
High effective heat-storage high-temperature cracking sewage, organic matter rubbish system
Technical field
The present invention relates to a kind of high effective heat-storage high-temperature cracking sewage, organic matter rubbish system, especially relate to by sewage, organic matter rubbish low energy consumption, it is aphlogistic under the conditions of be cracked into the device of hydrogen and oxygen gas mixture and normal temperature fuel gas.Prior art
So far, lioh hydrolysis is only limited to electrolytic method, and this is the huge method not having practical value of costly energy consumption.In order to change it is this disregard the tragedy phenomenon that Ecological Cost runs counter to the natural law, inventor according to
" the Nature closed cycle " is theoretical, summarizes the experience studied for many years, obtains the multinomial patent burnt on high-temperature cracking hydrogen and oxygen so far from 95 years, such as：Method for high temperature combustion of fuel（5) and a kind of top burning type Pintsch process organic matter of sewage garbage fired boiler 95112056.（ZL00205731. X. ).These new technical methods, be low energy consumption in the boiler will（0) sewage, organic matter rubbish, " Pintsch process " is distinguished into hydrogen and oxygen gas mixture and normal temperature fuel gas, traditional oil, coal, natural gas are instead of with hydrogen and oxygen gas mixture and normal temperature fuel gas, the conversion of the mechanical energy of one-kinetic energy of heat energy-one occurs in chemical combination and drives Turbo-generator Set to do work；Foregoing invention instead of " conventional conversion device " costly, energy consumption it is huge, pollution environment, etc. great insurmountable problem.
But in practice, high-temperature cracking hydrogen and oxygen burning boiler still suffers from many defects, such as because hydrogen-oxygen is explosive combustion, cause the shock wave that noise is big, flame sprays generation during operation big, safety coefficient is reduced, and has potential safety hazard, certain difficulty is brought to operation.The content of the invention
It is an object of the invention to provide a set of safer, noiseless, easily operated high effective heat-storage high-temperature cracking sewage, organic matter rubbish system.
The high effective heat-storage high-temperature cracking sewage of the present invention, organic matter rubbish system are made up of high effective heat-storage high-temperature cracking organic matter of sewage rubbish tank arrangement, heat-exchange device, closed cycle steam turbine, an equipressure level difference water injection device and pipeline and integrated circuit.
Described high effective heat-storage high-temperature cracking sewage, organic matter rubbish device, it is in being done by exotic material Serve as a contrast the upper and lower tank body with top dome of cylindrical type that is made up of metal material, tank body mainly by：Pintsch process sewage spiral coil, organic matter rubbish Pintsch process device, heat exchanger and note Xi Kou, Pai Xikou and four temperature controllers etc. are constituted；
Wherein respectively set a through hole at the upper and lower spherical center of binding of tank body, described cylindrical type tank body one side from top to bottom provided with nine through holes, be also respectively provided with a through hole the another side of cylindrical type tank body is upper and lower；
Via top is provided with the note Xi Kou being connected with tank body wherein on side, and the Pai Xikou by Valve controlling being connected with tank body is provided with the bottom of lower through-hole；
Described Pintsch process sewage spiral coil is located in tank body, by refractory metal material be made from top to bottom again by the upward spiral coil of lower spiral, wherein with tank body on the outside of first through hole be connected be：Pintsch process sewage spiral coil upper end by solenoid valve control high-pressure sewage entrance, second with the outer side through hole of tank body is connected is：Pintsch process sewage spiral coil upper end hydrogen-oxygen hybrid ionic gas vent；
Described organic matter rubbish Pintsch process device is located in tank body, and the hollow sphere being made up of refractory metal material is respectively provided with a through hole in the top of hollow sphere, middle side part, bottom；
Wherein through hole is connected with fuel gas spiral coil lower end at the top of organic matter rubbish Pintsch process device, and fuel gas spiral coil upper end is that the normal temperature fuel gas being connected with the 3rd through hole on the outside of tank body is exported；
The organic matter rubbish high pressure inlet that the through hole of organic matter rubbish Pintsch process device middle side part is connected with the other end with the 7th through hole on the outside of tank body is connected；
The through hole of organic matter rubbish Pintsch process device bottom and the other end and tank body outside, the connected inorganic matter rubbish high pressure extrusion of the 9th through hole are connected；
Four described temperature controllers are to be connected respectively with the 4th on the outside of tank body, the 5th, the 6th, the 8th through hole；
Described heat exchanger is located in tank body, the coil pipe being made up of refractory metal material, its upper end is the higher pressure steam outlet being connected with tank body opposite side upper through-hole, and its lower end is the water under high pressure inlet by solenoid valve control being connected with tank body opposite side lower through-hole；
Described heat-exchange device be by：Heat exchange spiral coil and two temperature controllers of peripheral hardware, pressure gauge, the safety valve set in heat exchange tank is constituted；
Described heat exchange tank is that the upper and lower tank body with top dome of cylindrical type is made by refractory metal material, and top dome portion is provided with two through holes provided with two through holes, lower top dome portion, upper and lower two through holes are additionally provided with the sorrowful face of tank body on heat exchange tank；
Described heat exchange spiral coil is located in heat exchange tank, and the spiral being made up of refractory metal material is changed Hot coil, wherein with first, heat exchange tank top dome portion through hole is connected is：The higher pressure steam inlet of spiral heat exchange pipe coil upper end, second with the through hole of heat exchange tank ball bottom centre is connected is：The condensation-water drain of spiral heat exchange pipe coil lower end；
Heat exchange tank top dome portion with second through hole is connected is：The higher pressure steam outlet and phase and pressure gauge even, safety valve by solenoid valve control of heat exchange tank；
Heat exchange tank ball bottom with second through hole is connected is：The water inlet by solenoid valve control of heat exchange tank；Heat exchange tank side with two through holes are connected is：Two temperature controllers of heat exchange tank；
Wherein described closed cycle steam turbine be by：Constituted in parts such as body, snail type impeller housing, impeller, bearing cap, main shaft and shaft couplings, it is characterised in that：
Two bodies of described closed cycle steam turbine are round, the uniform bolt holes in its neighboring, the also uniform bolt hole of circumferential edge is additionally provided with axis hole in the centre bearing groove of two type machines of circle, is divided into round two bodies and strengthen the body seat of gusset in the middle part of round two bodies；
The snail type impeller housing of described closed cycle steam turbine is that round aerial periphery sets outside groove, in the uniform cloth bolt hole of recessed circumferential, the external parallel that groove is set in snail type impeller housing bottom is provided with and the steam inlet communicated in groove and steam (vapor) outlet；
The impeller of described closed cycle steam turbine is to set multiple wheel posts in the axis hole neighboring for keyway, and periphery is gone back to outside wheel post and sets groove, by the oblique uniform blade of airintake direction in groove is set；
The bearing cap of described closed cycle steam turbine, one of bearing cap is that center sets through hole, the uniform bolt hole of circumferential edge, and another bearing cap is the uniform bolt hole of circumferential edge
Described closed cycle steam turbine is so assembled, and first fixes impeller by axle key with spindle set;The snail type impeller housing on impeller outer set, then two bodies are enclosed on main shaft and body are passed through one of by bolt bolt hole, the bolt hole of snail type impeller housing and the bolt hole of another body are fastened；Then two bearing holder (housing, cover)s are covered one of bearing cap and covers another bearing cap blending bolt again on axle and all screw tight the screw on bearing cap, be the shaft coupling with generator electric in the other end of main shaft;Described closed cycle steam turbine is made up of refractory metal material, the inside and outside sealing heat-proof device being thermally insulated.
Wherein described equipressure level difference water injection device is the housing for the hollow two ends top dome of column type for waiting pressure head injector to be made up of corrosion-resistant metal materials by two, two through holes are respectively set in housing top dome, bottom, top one through hole is the exhaust outlet by solenoid valve control, and another through hole is by the steam inlet of solenoid valve control；Bottom one through hole is the delivery port being connected with pressure water source by solenoid valve control, and another through hole is the water inlet by solenoid valve control； High effective heat-storage high-temperature cracking sewage of the present invention, organic matter rubbish system are so connected：
The high-pressure sewage entrance of Pintsch process sewage spiral coil in described high efficiency, heat storage, high temp cracking sewage organic garbage apptss tank body is connected by pipeline with high-pressure sewage pump discharge, and the hydrogen-oxygen hybrid ionic gas vent of Pintsch process sewage spiral coil is connected by pipeline with the air inlet of hydrogen or oxygen gas separator；
The normal temperature fuel gas outlet of the fuel gas spiral coil of organic matter rubbish Pintsch process device in described high efficiency, heat storage, high temp cracking sewage organic garbage apptss tank body is connected by pipeline with fuel gas transfer pipeline；The organic matter rubbish high pressure inlet of organic matter rubbish Pintsch process device is connected by pipeline with the outlet of organic matter rubbish high pressure extruder；The inorganic matter rubbish high pressure extrusion of organic matter rubbish Pintsch process device is connected by pipeline with without phase thing rubbish extruder entrance；
The higher pressure steam outlet of heat exchanger in described high efficiency, heat storage, high temp cracking sewage organic garbage apptss tank body is connected by pipeline with the higher pressure steam inlet of the heat exchange spiral coil set in heat-exchange device in heat exchange tank；
The condensation-water drain of the heat exchange spiral coil bottom set in heat-exchange device in heat exchange tank by pipeline and the discharge outlet that is controlled by electromagnetic valve and etc. pressure head injector bottom by the water inlet phase of solenoid valve control and company；The higher pressure steam outlet upper end by pressure gauge safety valve solenoid valve control in heat-exchange device at the top of heat exchange tank by pipeline and closed cycle steam turbine entrance and wait pressure head injector by the steam inlet phase of solenoid valve control and company；
The outlet of closed cycle steam turbine is connected by pipeline with steam conveying pipeline；
Exchanged heat in heat-exchange device pot bottom heat exchanger of the cold water inlet by solenoid valve control in pipeline and high efficiency, heat storage, high temp cracking sewage organic garbage apptss tank body by solenoid valve control water under high pressure inlet, etc. pressure head injector, bottom by the wealthy control of electromagnetism the delivery port being connected with pressure water source and be located at bottom by the discharge outlet phase of solenoid valve control and company；
The whole magnetic valves of high effective heat-storage high-temperature cracking sewage of the present invention, organic matter rubbish system and water level, pressure, temperature controller, all it is that alternately open and close are carried out by integrated circuit automatic control.
High efficiency, heat storage, high temp cracking sewage organic garbage apptss described in high effective heat-storage high-temperature cracking sewage of the present invention, organic matter rubbish system, it is inside and outside by thermal insulating coating heat-insulation and heat-preservation, and the tank body that liner is made up of metal material is done by exotic material, and the various devices and pipeline of whole system must all be made up of refractory metal material and by the heat-insulated processing of heat-barrier material.
High effective heat-storage high-temperature cracking sewage of the present invention, organic matter rubbish system, can according to design requirement by heat exchange tank in multiple heat-exchange devices and closed cycle steam turbine series combination into a greater amount of steam-electric power systems The high effective heat-storage high-temperature cracking sewage of the present invention, organic matter rubbish system, have the following advantages compared with prior art：1st, low cost；2nd, it is safer；3rd, it is noiseless；4th, it is without friction；5th, without flame；6th, it is easily operated；7th, low energy consumption；8th, heat energy is outwards exported.And can according to design requirement by heat exchange tank in multiple heat-exchange devices and closed cycle steam turbine series combination into a greater amount of steam generating systems.Brief description of the drawings
Fig. 1 is high effective heat-storage high-temperature cracking sewage of the present invention, organic matter rubbish system structure diagram.
Fig. 2 is the front view of turbine configuration in the present invention.
Fig. 3 is the side view of gas-turbine in the present invention.
Fig. 4 is the front view of the gas turbine impeller shell of the present invention.
Fig. 5 is the side view of the gas turbine impeller shell of the present invention.
Fig. 6 is the front view of the gas turbine impeller of the present invention.
Fig. 7 is the side view of the gas turbine impeller of the present invention.Best mode for carrying out the invention
The high effective heat-storage high-temperature cracking sewage of the present invention, organic matter rubbish system, are made up of high effective heat-storage high-temperature cracking organic matter of sewage rubbish tank arrangement, heat-exchange device, closed cycle steam turbine, an equipressure level difference water injection device and pipeline and integrated circuit.
High efficiency, heat storage, high temp cracking sewage organic garbage apptss shown in Figure 1, described, it is to do the upper and lower tank body 47 with top dome of cylindrical type that liner is made up of metal material by exotic material, tank body 47 mainly by：Pintsch process sewage spiral coil 42, organic matter rubbish Pintsch process device 50, heat exchanger 38 and note tin mouthfuls 36, row's tin mouthful 56 and four temperature controllers etc. are constituted；
Wherein respectively set a through hole at the upper and lower spherical center of binding of tank body 47, described cylindrical type tank body 47 one side from top to bottom provided with nine through holes, the another side of cylindrical type tank body 47 it is upper and lower be also respectively provided with-individual lead to lonely L;
Via top is provided with the note tin mouthful 36 being connected with tank body 47 wherein on side, and the row's tin mouthful 56 by Valve controlling being connected with tank body 47 is provided with the bottom of lower through-hole;
Described Pintsch process sewage spiral coil 42 is located in tank body 47, by refractory metal material be made from top to bottom again by the upward spiral coil of lower spiral, wherein with first through hole in the outside of tank body 47 is connected is：The upper end of Pintsch process sewage spiral coil 42 by solenoid valve control high-pressure sewage entrance 40, second with the outer side through hole of tank body 47 is connected is：The upper end hydrogen-oxygen hybrid ionic of Pintsch process sewage spiral coil 42 Gas vent 41;
Described organic matter rubbish Pintsch process device 50 is located in tank body 47, and the hollow sphere being made up of refractory metal material is respectively provided with a through hole in the top of hollow sphere, middle side part, bottom；
Wherein the top through hole 49 of organic matter rubbish Pintsch process device 50 is connected with the lower end of fuel gas spiral coil 45, and the upper end of fuel gas spiral coil 45 is the normal temperature fuel gas outlet 43 being connected with the 3rd through hole in the outside of tank body 47;
The organic matter rubbish high pressure inlet 51 that the 7th through hole of the through hole 52 of the middle side part of organic matter rubbish Pintsch process device 50 and the other end and the outside of tank body 47 is connected is connected；
The through hole 53 of the bottom of organic matter rubbish Pintsch process device 50 and the other end and the outside of tank body 47, the connected inorganic matter rubbish high pressure extrusion 55 of the 9th through hole are connected；
Described temperature controller 44,46,48,54 is to be connected respectively with the 4th on the outside of tank body 47, the 5th, the 6th, the 8th through hole；
Described heat exchanger 38 is located in tank body 47, the coil pipe being made up of refractory metal material, its upper end is the higher pressure steam outlet 37 being connected with the opposite side upper through-hole of tank body 47, and its lower end is the water under high pressure inlet 39 by solenoid valve control being connected with the opposite side lower through-hole of tank body 47;
Described heat-exchange device be by：Heat exchange spiral coil 17 and two temperature controllers of peripheral hardware, pressure gauge, the safety valve set in heat exchange tank 18 is constituted；
Described heat exchange tank 18 is that the upper and lower tank body with top dome of cylindrical type is made by refractory metal material, and top dome portion is additionally provided with upper and lower two through holes provided with two through holes, lower top dome portion provided with two through holes, in tank body side on heat exchange tank 18；
Described heat exchange spiral coil 17 is located in heat exchange tank 18, the spiral heat exchange pipe coil 17 being made up of refractory metal material, wherein with first, 18 top dome portion of heat exchange tank through hole is connected is：The higher pressure steam inlet 16 of the upper end of spiral heat exchange pipe coil 17, second condensation-water drain 22 for the-lower end of spiral heat exchange pipe coil 17 for being connected with the through hole of the ball bottom centre of heat exchange tank 18;
The top dome portion of heat exchange tank 18 with second through hole is connected is：The higher pressure steam outlet 12 and phase and pressure gauge 19 even, safety valve 27 by solenoid valve control of heat exchange tank 18;
The ball bottom of heat exchange tank 18 with second through hole is connected is：The water inlet 23 by solenoid valve control of heat exchange tank 18;
The side of heat exchange tank 18 with two through holes are connected is：The temperature controller 11,21 of heat exchange tank 18；Wherein described equipressure level difference water injection device is that pressure head injector 1,2 is waited by two by corrosion resistant metal
' the housing of the hollow two ends top dome of column type that is made of material, two through holes, top are respectively set in housing top dome, bottom One through hole is the exhaust outlet 3,6 by the wealthy control of electromagnetism, and another through hole is by the steam inlet 4,5 of solenoid valve control；Bottom one through hole is the delivery port 7,9 being connected with pressure water source 11 by solenoid valve control, and another through hole is the water inlet 8,10 by solenoid valve control；
Fig. 2 to Fig. 7 is the structural representation of closed cycle steam turbine (14) in high effective heat-storage high-temperature cracking sewage of the present invention, organic matter rubbish system；Closed cycle steam turbine (14) is described in detail with reference to Fig. 2 to Fig. 7;Wherein described closed cycle steam turbine 14 be by：Constituted in parts such as body, snail type impeller housing, impeller, bearing cap, main shaft and shaft couplings, it is characterised in that：
The body 141,148 of described closed cycle steam turbine is round, the uniform bolt hole 142 in its neighboring, is additionally provided with axis hole in the centre bearing groove of round machine 141,148 in circular main body 141, the also uniform bolt hole 151 of 148 middle part circumferential edges, divided into circular main body 141,148 and strengthen the body seat 146 of gusset;The snail type impeller housing 153 of described closed cycle steam turbine is that round aerial periphery sets outside groove, in the uniform cloth bolt hole 142 of recessed circumferential, the external parallel that groove is set in the bottom of snail type impeller housing 153 is provided with and the steam inlet 145 communicated in groove and steam (vapor) outlet 147;
The impeller 158 of described closed cycle steam turbine is to set multiple wheel posts 156 in the neighboring of axis hole 154 for keyway (159), groove 155 is set on the outer periphery of returning of wheel post 156, by the oblique uniform blade 157 of airintake direction in groove 155 is set;
The bearing cap of described closed cycle steam turbine, one of bearing cap 149 is that center sets through hole, the uniform bolt hole of circumferential edge, and another bearing cap 150 is the uniform bolt hole of circumferential edge
Described closed cycle steam turbine is so assembled, and impeller 158 is set with main shaft 144 is fixed by axle key first；The snail type impeller housing 153 on the outer set of impeller 158, then body 141,148 is enclosed on main shaft 144 and fastened by bolt hole 142, the bolt hole 142 of snail type impeller housing 153 and the bolt hole 142 of body 148 of bolt through body 141；Then bearing 152,154 is enclosed on axle to cover upper ball cover 149 again and cover the blending bolt of bearing cap 150 and all screws tight the screw on bearing cap, be the shaft coupling 143 with generator electric in the other end of main shaft 144;
Described closed cycle steam turbine is made up of refractory metal material, the inside and outside sealing heat-proof device being thermally insulated.
High effective heat-storage high-temperature cracking sewage of the present invention, organic matter rubbish system, are so connected：The high-pressure sewage entrance 40 of Pintsch process sewage spiral coil 42 in described high efficiency, heat storage, high temp cracking sewage organic garbage apptss tank body 47 is connected by pipeline with high-pressure sewage pump discharge, and the hydrogen-oxygen hybrid ionic gas vent 41 of Pintsch process sewage spiral coil 42 is connected by pipeline with the air inlet of hydrogen or oxygen gas separator；Organic matter rubbish high temperature in described high efficiency, heat storage, high temp cracking sewage organic garbage apptss tank body 47 The normal temperature fuel gas outlet 43 of the fuel gas spiral coil 45 of cracker 50 is connected by pipeline with fuel gas transfer pipeline；The organic matter rubbish high pressure inlet 51 of organic matter rubbish Pintsch process device 50 is connected by pipeline with the outlet of organic matter rubbish high pressure extruder；The inorganic matter rubbish high pressure extrusion 55 of organic matter rubbish Pintsch process device 50 is connected by pipeline with without phase thing rubbish extruder entrance；
The higher pressure steam outlet 37 of heat exchanger 38 in described high efficiency, heat storage, high temp cracking sewage organic garbage apptss tank body 47 is connected by pipeline with the higher pressure steam inlet 16 of the heat exchange spiral coil 17 set in heat exchange tank in heat-exchange device 18；
The condensation-water drain 22 of heat exchange spiral coil 17 bottom set in heat-exchange device in heat exchange tank 18 by pipeline and the discharge outlet 26 that is controlled by electromagnetic valve and etc. pressure head injector 1,2 bottoms by solenoid valve control water inlet 8,10 mutually and even；
In heat-exchange device the top of heat exchange tank 18 by pressure gauge 19, the solenoid valve control of safety valve 27 the upper end of higher pressure steam outlet 12 by pipeline and closed cycle steam turbine 14 entrance 145 and wait the steam inlet 4,5 by solenoid valve control of pressure head injector 1,2 mutually and company；
The outlet 147 of closed cycle steam turbine 14 is connected by pipeline with steam conveying pipeline；
In heat-exchange device heat exchanger 38 of the cold water inlet 23 by solenoid valve control of the bottom of heat exchange tank 18 in pipeline and high efficiency, heat storage, high temp cracking sewage organic garbage apptss tank body 47 by solenoid valve control high-pressure sewage inlet 39, etc. pressure head injector 1,2, bottom by solenoid valve control the delivery port 7,9 being connected with pressure water source 11 and be located at bottom by solenoid valve control discharge outlet phase simultaneously
The high effective heat-storage high-temperature cracking sewage, organic matter rubbish system is characterized in that：Whole system whole magnetic valves and water level, pressure, temperature controller, be all by the automatic control of integrated circuit 57 carry out alternately open and close.
The high effective heat-storage high-temperature cracking sewage, organic matter rubbish system is characterized in that：Described high efficiency, heat storage, high temp cracking sewage organic garbage apptss, it is inside and outside by thermal insulating coating heat-insulation and heat-preservation, and the tank body 47 that liner is made up of metal material is done by exotic material, and the various devices and pipeline of whole system must all be made up of refractory metal material and by the heat-insulated processing of heat-barrier material.
The work to high effective heat-storage high-temperature cracking sewage of the present invention, organic matter rubbish system is described in detail below：
First turning on the integrated circuit 57 of automaton makes the pressure water source capsule mouthful 11 by solenoid valve control, Deng the bottom of pressure head injector 1 by solenoid valve control cold water inlet 7, Deng the top of pressure head injector 1 by solenoid valve control air bleeding valve 3, Deng the bottom of pressure head injector 1 by solenoid valve control delivery port 8, and the bottom of heat exchange tank 18 coupled by the road by cold water inlet 23 and heat exchange tank 18 top of solenoid valve control by solenoid valve control steam (vapor) outlet 22, by pipeline with waiting the top of pressure head injector 1 by the steam of solenoid valve control Entrance 4 etc., above all of valve is opened simultaneously automatically；
There are the bottoms of pressure head injector 1 such as pressure cold water to enter by the road in heat exchange tank 18 because of water-head, the air in heat exchange tank 18 is forced out by the steam (vapor) outlet at top through the pressure head injector 1 such as pipe entrance top, then by the air bleeding valve doorway at top；Treat that water level reaches water level in heat exchange tank 18, pressure, temperature-controlled instrument is restricted water supply position, it is first shut off automatically by the steam (vapor) outlet 12 of solenoid valve control at the top of the cold water inlet 23 and heat exchange tank 18 by solenoid valve control of the bottom of heat exchange tank 18, when waiting the water level in pressure head injector 1 also to reach to restrict water supply, there is the pressure saline source mouth of pipe 11 by solenoid valve control, Deng the bottom of pressure head injector 1 by solenoid valve control cold water inlet 7, also closed automatically by the delivery port 8 of solenoid valve control by the bottom of the grade pressure head of air bleeding valve 3 injector 1 of solenoid valve control Deng the top of pressure head injector 1；
Tin is heated to 1500 or so, out of, the top of high efficiency, heat storage, high temp cracking sewage organic garbage apptss tank body 47 the injection tank body 47 of tin entrance 36；
It is then turned on integrated circuit 57, via integrated circuit 57 control the continual upper end of Pintsch process sewage spiral coil 42 into high efficiency, heat storage, high temp cracking sewage organic garbage apptss tank body 47 of high-pressure sewage pump by solenoid valve control the quantitative injection of high-pressure sewage entrance 40, sewage instant vaporization at a high temperature of 1500 °C or so, into saturated vapor, and continues to be cracked into the destructive distillation steam of superheated steam one（" Carnot cycle " thinks impossible gas）- one " perfect gas "（" hydroxyl ion stream ")；The chemical combination one that the air-flow is carried out many times in Pintsch process sewage spiral coil 42 is cracked discharges the high temperature that oxyhydroxide reaction is produced into high efficiency, heat storage, high temp cracking sewage organic garbage apptss tank body 47 during chemical combination is cracked again and again again and again, raise temperature moment in high efficiency, heat storage, high temp cracking sewage organic garbage apptss tank body 47, " hydroxyl ion stream " enters the air inlet of hydrogen or oxygen gas separator after the cracking of chemical combination one many times through the upper end hydrogen-oxygen hybrid ionic gas vent 41 of Pintsch process sewage spiral coil 42, and continual separated by hydrogen-oxygen stores in the device；
When temperature in high efficiency, heat storage, high temp cracking sewage organic garbage apptss tank body 47 is raised, integrated circuit 57 would automatically turn on organic matter rubbish high pressure extruder, and making organic matter rubbish continual, the height of organic matter rubbish high pressure inlet 51 through the organic matter rubbish Pintsch process device 50 in high efficiency, heat storage, high temp cracking sewage organic garbage apptss tank body 47 is pressed into；In organic matter rubbish Pintsch process device 50, machine thing rubbish in high temperature by transient evaporation into normal temperature fuel gas, from the normal temperature fuel gas outlet 43 of the fuel gas spiral coil 45 at the top of organic matter rubbish Pintsch process device 50 by Pipeline transport into fuel gas transfer pipeline；It is continual in the apparatus to be extruded and inorganic matter rubbish high pressure extrusion 55 of the inorganic matter being cleaved in organic matter rubbish Pintsch process device 5 through the bottom of organic matter rubbish Pintsch process device 5 is entered without phase thing rubbish extruder entrance by pipeline；
Simultaneously, the temperature in high efficiency, heat storage, high temp cracking sewage organic garbage apptss tank body 47 is continuous Improving, the heat exchanger 38 for being located at the inner top of high efficiency, heat storage, high temp cracking sewage organic garbage apptss tank body 47 that integrated circuit 57 is controlled is automatically turned on by the water under high pressure inlet 39 of solenoid valve control, high-pressure cold water is high steam in the instant vaporization of heat exchanger 38, the steam inlet 16 for the upper end of spiral heat exchange pipe coil 17 that the high steam of heat exchanger 38 enters in heat exchange tank 18 from higher pressure steam outlet 37 by the road, the principle of " closed cycle " is pressed in into the spiral heat exchange pipe coil 17 in heat exchange tank 18, from top to bottom the temperature difference is carried out with the cold water in heat exchange tank 18 to exchange, steam in spiral heat exchange pipe coil 17 be condensed into condensed water through the lower end of spiral heat exchange pipe coil 17 by the condensation-water drain 22 of solenoid valve control by the road from waiting bottom of pressure head injector 2 to enter the air bleeding valve for the top of pressure head injector 2 such as having automatically turned on by solenoid valve control by the water inlet 10 of solenoid valve control
In 6 grade pressure head injector 2；
The cold water of the inner top of heat exchange tank 18 is in temperature difference exchange, it is vaporizated into high steam, higher pressure steam outlet 12 from the top of heat exchange tank 18 is promoted the wheel rotation in closed cycle steam turbine 14, is driven generator acting by pipeline and the entrance 13 for entering closed cycle steam turbine 14；
Simultaneously the higher pressure steam outlet 12 at the top of heat exchange tank 18 also enter by the road the top of the pressure head such as people injector 1 by the steam inlet 4 of solenoid valve control, etc. the bottom of pressure head injector 1 automatically turned on again by the delivery port 7 of solenoid valve control, the steam inlet by solenoid valve control for the pressure head injector 1 such as enter high steam
4, reciprocity pressure head injector 1 is interior to be pressurized, and is made heat exchange tank 18 and is waited pressure head injector 1 to keep isobaric, waits pressure head injector 1 to make because of potential difference in water injection heat exchange tank 18；
When waiting, the note of the hydraulic pressure in pressure head injector 1 is most, Deng the top of pressure head injector 1 by the steam inlet 4 of solenoid valve control, etc. the bottom of pressure head injector 1 by solenoid valve control delivery port 7 it is automatic again close, wait the top of pressure head injector 1 by solenoid valve control exhaust outlet 3, etc. cold water inlet 8 of the bottom of pressure head injector 1 by solenoid valve control and the automatic opening simultaneously of pressure water source capsule mouthful 11 by solenoid valve control；
And wait the top of pressure head injector 2 by the steam inlet 5 of solenoid valve control, etc. the bottom of pressure head injector 2 automatically turned on by the delivery port 9 of solenoid valve control, wait the bottom of pressure head injector 2 to be closed automatically by the cold water inlet 10 of solenoid valve control；Hydraulic pressure note in pressure head injector 2 to be waited to the greatest extent, waits the water in pressure head injector 1 to automatically continue cycle alternation again and the water that required evaporation is supplemented into heat exchange tank 18；
The high effective heat-storage high-temperature cracking sewage, organic matter rubbish system is characterized in that：Can according to design requirement by heat exchange tank 17 in multiple heat-exchange devices and the series combination of closed cycle steam turbine 14 into a greater amount of steam generating systems.Industrial applicability
High effective heat-storage high-temperature cracking sewage that the present invention is provided, organic matter rubbish system, compared with prior art Cost is lower, safer, noiseless, without friction, can export without flame, easily operated, low energy consumption and outwards heat energy.And can according to design requirement by heat exchange tank in multiple heat-exchange devices and closed cycle steam turbine series combination into a greater amount of steam generating systems, suitable for industrial application.

Claims (1)

  1. Claim
    1st, high effective heat-storage high-temperature cracking sewage, organic matter rubbish system, it is characterised in that：It is to be made up of high efficiency, heat storage, high temp cracking sewage organic garbage apptss, heat-exchange device, closed cycle steam turbine, an equipressure level difference water injection device and pipeline and integrated circuit；
    The high efficiency, heat storage, high temp cracking sewage organic garbage apptss, are to do the upper and lower tank body with top dome of cylindrical type that liner is made up of metal material by exotic material（47), tank body（47) mainly by Pintsch process sewage spiral coil（42), organic matter rubbish Pintsch process device（50), heat exchanger（38) with note Xi Kou (36), Pai Xikou（And four temperature controllers are constituted 56)；
    Wherein in tank body（47) upper and lower spherical center of binding respectively sets a through hole, the note Xi Kou（36) it is located at tank body（47) top, Pai Xikou（56) it is located at tank body（47) bottom, by Valve controlling；In described cylindrical type tank body（47) one side is from top to bottom provided with nine through holes, in cylindrical type tank body（47) another side is upper and lower to be also respectively provided with a through hole；
    The Pintsch process sewage spiral coil（42) it is located at tank body（47) in, be by refractory metal material be made from top to bottom again by the upward spiral coil of lower spiral, its upper end by solenoid valve control high-pressure sewage entrance（And tank body 40)（47) first, outside through hole is connected, its upper end hydrogen-oxygen hybrid ionic gas vent（41) it is connected with second through hole on the outside of tank body (47)；
    The organic matter rubbish Pintsch process device（50) it is located at tank body（47) in, it is the hollow sphere being made up of refractory metal material, a through hole is respectively provided with the top of hollow sphere, middle side part, bottom；Through hole at the top of wherein（49) with being located at tank body（47) the fuel gas spiral coil in（45) lower end is connected, fuel gas spiral coil（45) upper end exports for normal temperature fuel gas（43), with tank body（47) the 3rd, outside through hole is connected；Organic matter rubbish Pintsch process device（50) through hole of middle side part（52) it is connected to organic matter rubbish high pressure inlet（51), the mouth（51) other end and tank body（47) the 7th, outside through hole is connected；Organic matter rubbish Pintsch process device（50) through hole of bottom（53) inorganic matter rubbish high pressure extrusion (55), the outlet are connected to（55) other end and tank body（47) the 9th, outside through hole is connected；
    The temperature controller（44)、 （46)、 （48), (54) respectively with tank body（47) the 4th on the outside of, the 5th, the 6th, the 8th through hole be connected；
    The heat exchanger（38) it is located at tank body（47) it is the coil pipe being made up of refractory metal material, the higher pressure steam outlet of its upper end in（And tank body 37)（47) opposite side upper through-hole be connected, its lower end by solenoid valve control water under high pressure inlet（And tank body 39)（47) opposite side lower through-hole is connected；
    The heat-exchange device, is by heat exchange tank（18) the heat exchange spiral coil set in（And peripheral hardware 17) Two temperature controllers, pressure gauge, safety valve constitute；
    Wherein described heat exchange tank（18) it is the upper and lower tank body with top dome of cylindrical type that is made up of refractory metal material, in heat exchange tank（18) top dome portion is additionally provided with upper and lower two through holes provided with two through holes, lower top dome portion provided with two through holes, in tank body side on；
    The heat exchange spiral coil（17) it is located at heat exchange tank（18) in, it is made up of refractory metal material, its upper end is higher pressure steam inlet（16), with heat exchange tank（18) first, top dome portion through hole is connected, and its lower end is condensation-water drain (22), with heat exchange tank（18) second through hole of ball bottom centre is connected；
    Heat exchange tank（18) second through hole connection higher pressure steam outlet in top dome portion（12) with phase and pressure gauge even（19), safety valve（27);
    Heat exchange tank（18) second through hole of ball bottom connects the water inlet by solenoid valve control（23 );
    Heat exchange tank（18) two through holes in side are respectively communicated with temperature controller（11 )、 （21 );
    The closed cycle steam turbine (14) is made up of parts such as body, snail type impeller housing, impeller, bearing cap, main shaft and shaft couplings：
    The body (141) of described closed cycle steam turbine,（148) it is round, the uniform bolt hole in its neighboring（142), circular main body (141),（148) the middle part also uniform bolt hole of circumferential edge（151), the centre bearing groove in circular main body (141), (148) is additionally provided with axis hole（144) the body seat (146) for strengthening gusset, is divided into circular main body (141), (148);
    The snail type impeller housing of described closed cycle steam turbine（153) it is that round hollow periphery sets outside groove, in the uniform bolt hole of recessed circumferential（142), in snail type impeller housing（153) bottom sets the external parallel of groove provided with the steam inlet with being communicated in groove（And steam (vapor) outlet 145)（147);
    The impeller (158) of described closed cycle steam turbine is to set multiple wheel posts (156) in axis hole (154) neighboring for keyway (159), in wheel post（156) neighboring sets groove（155), in groove（155) the oblique uniform blade (157) of airintake direction is pressed in;
    The bearing cap of described closed cycle steam turbine is two, one of bearing cap（149) through hole, the uniform bolt hole of circumferential edge, another bearing cap are set at center（150) in the uniform bolt hole of circumferential edge；Described closed cycle steam turbine is so assembled, first by impeller (158) and main shaft（144) suit is fixed by axle key；In impeller (158) outside, snail type impeller housing is put（153), then by body (141), (148) it is enclosed on main shaft（144) bolt hole of body (141) is passed through on and by bolt（142), snail type impeller housing（153) bolt hole（142) with the bolt hole of body (148)（142) fastened；Then by bearing（152), (154) are enclosed on axle covers upper ball cover again（149) with the bearing cap covered（150) blending bolt all screws tight the screw on bearing cap, in main shaft（144) the other end is the connection with generator Axle device (143) is connected；
    Described closed cycle steam turbine is made up of refractory metal material, the inside and outside sealing device being thermally insulated.
    Wherein described equipressure level difference water injection device is to wait pressure head injector by two（1) housing for the hollow two ends top dome of column type that, (2) are made up of corrosion-resistant metal materials, two through holes are respectively set in housing top dome, bottom, and top one through hole is the exhaust outlet by solenoid valve control（3)、 （6), another through hole is by the steam inlet of solenoid valve control（4)、 (5)；Bottom one through hole is by solenoid valve control and pressure water source（11) connected delivery port（7)、 （9), another through hole is the water inlet by solenoid valve control（8)、 ( 10)；
    2nd, high effective heat-storage high-temperature cracking sewage, organic matter rubbish system according to claim 1, it is characterised in that：
    Described high efficiency, heat storage, high temp cracking sewage organic garbage apptss tank body（47) the Pintsch process sewage spiral coil in（42) high-pressure sewage entrance（40) it is connected by pipeline with high-pressure sewage pump discharge, Pintsch process sewage spiral coil（42) hydrogen-oxygen hybrid ionic gas vent（41) it is connected by pipeline with the air inlet of hydrogen or oxygen gas separator；
    Described high efficiency, heat storage, high temp cracking sewage organic garbage apptss tank body（47) the organic matter rubbish Pintsch process device in（50) fuel gas spiral coil（45) normal temperature fuel gas outlet（43) it is connected by pipeline with fuel gas transfer pipeline；Organic matter rubbish Pintsch process device（50) organic matter rubbish high pressure inlet（51) it is connected by pipeline with the outlet of organic matter rubbish high pressure extruder；Organic matter rubbish Pintsch process device（50) inorganic matter rubbish high pressure extrusion（55) it is connected by pipeline with inorganic matter rubbish extruder entrance；Described high efficiency, heat storage, high temp cracking sewage organic garbage apptss tank body（47) heat exchanger in（38) higher pressure steam outlet（37) heat exchange tank in pipeline and heat-exchange device（18) the heat exchange spiral coil set in（17) higher pressure steam inlet（16) it is connected；
    Heat exchange tank in heat-exchange device（18) the heat exchange spiral coil set in（17) condensation-water drain (22) of bottom is by pipeline and the discharge outlet by the wealthy gate control of electromagnetism（26) with grade pressure head injector（1), (2) bottom by solenoid valve control water inlet（8), (10) Xiang Binglian；
    Heat exchange tank in heat-exchange device（18) at the top of by pressure gauge（19), safety valve（27) higher pressure steam outlet of solenoid valve control（12) upper end is by pipeline and closed cycle steam turbine（14) entrance（145) and pressure head injector is waited（1), the steam inlet by solenoid valve control of (2)（4), (5) Xiang Binglian；Closed cycle steam turbine（14) outlet（147) it is connected by pipeline with steam conveying pipeline；Heat exchange tank in heat-exchange device（18) cold water inlet by solenoid valve control of bottom（23) by pipeline and high efficiency, heat storage, high temp cracking sewage organic garbage apptss tank body（47) heat exchanger in（38) by The water under high pressure inlet of solenoid valve control（, 39) the pressure head injector such as（1 )、 （2), bottom is by solenoid valve control and pressure water source（11) connected delivery port（7), (9) and bottom is located at by the discharge outlet phase of solenoid valve control and company；
    3rd, high effective heat-storage high-temperature cracking sewage according to claim 1 or claim 2, organic matter rubbish system, it is characterised in that：Whole system whole magnetic valves and water level, pressure, temperature controller, all it is by integrated circuit（57) automatic control carries out alternately open and close.
    4th, high effective heat-storage high-temperature cracking sewage, organic matter rubbish system according to claim 1 or 2 or 3, it is characterised in that：Described high efficiency, heat storage, high temp cracking sewage organic garbage apptss, it is inside and outside by thermal insulating coating heat-insulation and heat-preservation, and does the tank body that liner is made up of metal material by exotic material（, and the various devices and pipeline of whole system must all be made up of refractory metal material and by the heat-insulated processing of heat-barrier material 47).
    5th, high effective heat-storage high-temperature cracking sewage, organic matter rubbish system according to claim 1 or 2,3,4, it is characterised in that：Can be according to design requirement by heat exchange tank in multiple heat-exchange devices（And closed cycle steam turbine 17)（14) series combination is into a greater amount of steam generating systems.
CNB038122731A 2002-04-30 2003-04-29 High performance heat storage high temperature system for decomposition of effluent and organic garbage Expired - Fee Related CN1318802C (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
CN02116732.X 2002-04-30
CN02116732 2002-04-30
PCT/CN2003/000317 WO2003093726A1 (en) 2002-04-30 2003-04-29 High efficiency and high temperature cracking system with heat storage for sewage and organic garbage

Publications (2)

Publication Number Publication Date
CN1656340A true CN1656340A (en) 2005-08-17
CN1318802C CN1318802C (en) 2007-05-30

Family

ID=29276006

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB038122731A Expired - Fee Related CN1318802C (en) 2002-04-30 2003-04-29 High performance heat storage high temperature system for decomposition of effluent and organic garbage

Country Status (3)

Country Link
CN (1) CN1318802C (en)
AU (1) AU2003234891A1 (en)
WO (1) WO2003093726A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101713304B (en) * 2009-09-30 2013-05-29 陈小刚 Method for cycle power generation by carrying out wet decomposition pretreatment, dry distillation and gasification on domestic garbage

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2321784B1 (en) * 2006-09-27 2010-03-17 Nicolas Correa Service, S.A. ENERGY GENERATOR INSTALLATION FROM BIOMASS.
CN109631048B (en) * 2018-12-26 2019-12-24 福建省凯圣生物质发电有限公司 Biomass energy recovery method

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0978072A (en) * 1995-09-11 1997-03-25 Komatsu Ltd Decomposition of waste plastics and apparatus therefore
CN1079525C (en) * 1998-05-05 2002-02-20 韩连恩 Gasification method for city garbage and garbage gasification furnace
CN2441081Y (en) * 2000-02-21 2001-08-01 林茂森 Top combustion style boiler for high temperature pyrolizing organic materials, sewage and garbage

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101713304B (en) * 2009-09-30 2013-05-29 陈小刚 Method for cycle power generation by carrying out wet decomposition pretreatment, dry distillation and gasification on domestic garbage

Also Published As

Publication number Publication date
CN1318802C (en) 2007-05-30
AU2003234891A1 (en) 2003-11-17
WO2003093726A1 (en) 2003-11-13

Similar Documents

Publication Publication Date Title
CN101288963B (en) Wood electrothermal high-temperature processing device and heat treating device with combination drying function
CN201257698Y (en) Lignum electrothermic high-temperature processing equipment and heat processing machine with federation dry function
CN105114266B (en) Power device using heat pump technology
CN1656340A (en) High performance heat storage high temperature system for decomposition of effluent and organic garbage
CN102304235B (en) High-temperature feeding and deslagging cracker for waste rubber and waste plastic
CN110194580A (en) A kind of greasy filth resource utilization system and technique
CN205653405U (en) Superheated steam carbide furnace
CN201335363Y (en) Fuel gas steam engine
CN100462526C (en) Heat regenerative engine
CN209398470U (en) New high-efficiency combined cycle drive system applied to large-scale lighter hydrocarbons deep processing
CN104566316B (en) Steam engine and steam generating system
CN209013167U (en) High-temperature steam generator
CN201695000U (en) Sludge treatment system
CN102094707B (en) Hydrogen energy vortex engine
CN206803094U (en) A kind of vaporising device of waste heat boiler
CN205717844U (en) A kind of energy-saving type boiler
CN220083042U (en) Exhaust-heat boiler externally-discharged steam recycling device
CN212108338U (en) Energy-concerving and environment-protective type steam generator
CN2756960Y (en) High efficiency heat storage high temperature cracking device
CN219530964U (en) Thermal power circulating water heating device
CN201421069Y (en) Fuel gas steam engine
CN218846109U (en) Steam-water circulation structure of waste heat boiler
CN216632031U (en) Carbonization equipment based on heterotopic thermal desorption
CN213363287U (en) Waste heat utilization device of drying chamber
CN211999878U (en) Reducing furnace for hot galvanizing processing of steel pipe

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20070530

Termination date: 20090601