CN103897713B - A kind of organic materials total system and treatment process - Google Patents

A kind of organic materials total system and treatment process Download PDF

Info

Publication number
CN103897713B
CN103897713B CN201210573421.4A CN201210573421A CN103897713B CN 103897713 B CN103897713 B CN 103897713B CN 201210573421 A CN201210573421 A CN 201210573421A CN 103897713 B CN103897713 B CN 103897713B
Authority
CN
China
Prior art keywords
gas
carbonization
organic materials
tower
washing
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.)
Active
Application number
CN201210573421.4A
Other languages
Chinese (zh)
Other versions
CN103897713A (en
Inventor
隋建国
由甲
由里
隋荣恒
吴班
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.)
SHANDONG HI-LINK ELECTRICITY Co Ltd
Original Assignee
SHANDONG HI-LINK ELECTRICITY Co Ltd
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 SHANDONG HI-LINK ELECTRICITY Co Ltd filed Critical SHANDONG HI-LINK ELECTRICITY Co Ltd
Priority to CN201210573421.4A priority Critical patent/CN103897713B/en
Publication of CN103897713A publication Critical patent/CN103897713A/en
Application granted granted Critical
Publication of CN103897713B publication Critical patent/CN103897713B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

Organic materials integrated conduct method of the present invention, comprises the following steps: the elementary screening of A. material, removes a small amount of heavy seeds based on metal, and then light material carries out fragmentation pulverizing; B. mixing of materials forming processes; C. material enters organic materials carbonization gasified boiler and carries out destructive distillation, discharges half smokeless fuel product and carbonizing gas; D. carbonizing gas carries out elementary washing, purifying through elementary carbonization gas washing tower, removes the dust, the mink cell focus that carry; Then carry out secondary washing purification through secondary carbonization gas washing tower, remove most of lightweight oil in gas; E. after washing, gas carries out two-stage de-oiling, dehydration, cooling, desulfurization, de-naphthalene through self-cleaning interchanger, obtains the carbonizing gas that clean combustiblecomponents is methane, carbon monoxide, hydrogen.The invention has the beneficial effects as follows, easy to use, cost is low, do not produce Dioxins and heavy metal free pollutes, without waste residue, the solid of output is as half smokeless fuel.

Description

A kind of organic materials total system and treatment process
Technical field
The present invention relates to a kind of for organic materials total system and treatment process.
Background technology
For domestic refuse, the burning disposal mode adopted at present can produce the products such as dioxin, heavy metal contamination, waste residue, causes environmental pollution.And need oil spout combustion-supporting in burning disposal process, directly cause processing cost too high.
Summary of the invention
The present invention is in order to make up the deficiencies in the prior art, provide a kind of easy to use, do not produce dioxin (adopting low temperature pyrogenation retorting technique temperature to control within 500 DEG C in treatment process process), heavy metal contamination, waste residue, lower-cost organic materials total system and treatment process.
The present invention is achieved through the following technical solutions:
Organic materials integrated conduct method of the present invention, its special character is: comprise the following steps:
A. the elementary screening of material, removes a small amount of heavy seeds based on metal, and then light material carries out fragmentation pulverizing;
B. mixing of materials forming processes;
C. material enters organic materials carbonization gasified boiler and carries out destructive distillation, discharges half smokeless fuel product and carbonizing gas;
D. carbonizing gas carries out elementary washing, purifying through elementary carbonization gas washing tower, removes the dust, the mink cell focus that carry; Then carry out secondary washing purification through secondary carbonization gas washing tower, remove most of lightweight oil in gas;
E. after washing, gas carries out elementary de-oiling, dehydration, cooling through self-cleaning interchanger, the lightweight oil that self-cleaning system produces and weakly alkaline liquid carry out desulfurization, de-naphthalene to gas, then through another self-cleaning interchanger de-oiling again, dehydration, desulfurization, de-naphthalene, cooling process, the carbonizing gas that clean combustiblecomponents is methane, carbon monoxide, hydrogen is obtained.
Organic materials integrated conduct method of the present invention, also comprise step F: the condensation mixed solution after elementary washing, purifying enters condensate circulation pond, through settlement separate go out dust, tar, after being separated, the water of natural subsidence reenters elementary carbonization gas washing tower and carries out wash cooling to gas, recycles; Gas after initial wash continues to enter secondary carbonization gas washing tower, self-cleaning interchanger, the recirculated water lower by temperature again washs gas, lowers the temperature, phlegma after washing flows into circulation settling bowl, settlement separate de-oiling again, imurity-removal process, the water after precipitate and separate enters systemic circulation and uses; Tar timing after sedimentation is drawn to outside oil tank sells.
In steps A, strip-type screen is used to screen out a small amount of heavy seeds based on metal, then by light material fragmentation in advance, be crushed within 8 millimeters again.
In step B, with shaping equipment, comminuting matter is prepared into the material of 10-100 millimeter.
In step C, in carbonizing gas, combustible gas composition is methane, carbon monoxide, hydrogen.Adopt low temperature pyrogenation retorting technique in treatment process process, temperature controls within 500 DEG C.
Organic materials total system of the present invention, is characterized in that: comprise the Supplying Sieving Mechanism, material crushing device, material forming device, organic materials carbonization gasified boiler, elementary carbonization gas washing tower, secondary carbonization gas washing tower, the self-cleaning interchanger that set gradually.
Self-cleaning interchanger comprises the square tube shape gas compartment of above-below direction, the gas converting heat pipe of a large amount of transverse directions is provided with in gas compartment, recirculated cooling water is had in gas converting heat pipe, be provided with gas inlet strainer bottom gas compartment and connect gas inlet pipe, gas compartment top has clean gas to export and weak base desulfurizing scrubber, and phlegma relief outlet is positioned at bottom gas compartment; Gas converting heat pipe top is also provided with Wen and flutters day with fog and self-cleaning uniform divider, is provided with the some heat exchange tower trays for uniform gas in gas converting heat pipe; Clean gas exports, Wen flutters day with fog, weak base desulfurizing scrubber, self-cleaning uniform divider, heat exchange tower tray are arranged in order from top to bottom.
The nesting box that Organic material gasification furnace comprises body of heater, is arranged on the top feed bin at body of heater top, bottom of furnace body correspondence is arranged; In body of heater, bottom is provided with the organic materials oxidation of several above-below directions side by side, destructive distillation, kiln, each organic materials oxidation, destructive distillation, kiln lower end are provided with automatic discharging device, are provided with combustion air inlet mouth between adjacent two organic materials oxidations, destructive distillation, kiln; Body of heater internal upper part is provided with carbonizing gas and collects and draw the mouth of pipe and gas and diffuse uniform distributor and gas collection device in interface, vapourizing furnace; The wall of organic materials oxidation, destructive distillation, kiln is provided with combustion chamber down cycles water jacket.
Elementary carbonization gas washing tower of the present invention, comprise carbonization gas entrance and carbonization gas outlet, top is provided with recirculated water spray line, and middle part is provided with Venturi meter and large Venturi meter, and bottom is provided with flashback tank.Flashback tank is provided with phlegma tar overflow port.Recirculated water spray line top is provided with recirculated water distributor disk, and recirculated water distributor disk is provided with recirculated water water-in.Elementary carbonization gas washing tower can remove most of dust, mink cell focus in carbonizing gas.
Secondary carbonization gas washing tower of the present invention, comprise carbonization gas inlet duct and carbonization gas outlet conduit, be provided with the tower tray of a large amount of transverse directions in tower body from top to bottom, gas flows from the gap between tower tray, be provided with recirculated water spray line in the middle part of tower body, bottom tower body, be provided with phlegma liquid discharge pipe.Cleanout opening is had bottom tower body.Phlegma liquid discharge pipe connects phlegma water seal cylinder, and phlegma water seal cylinder is provided with phlegma tar spillway.Secondary carbonization gas washing tower can remove the lightweight oil in carbonizing gas and be unfavorable for the portion gas of burning.
The invention has the beneficial effects as follows, easy to use, cost is low, for domestic refuse, compared with the existing processing mode of burning away the refuse generally adopted, it does not produce Dioxins and heavy metal free pollutes, without waste residue after process, the solid of output is as half smokeless fuel, its calorific value is more than per kilogram 5000 kilocalorie, and simultaneously output is used for the carbonizing gas that generates electricity, and calorific value is more than every cubic metre of 1200 kilocalories.Be suitable for material scope: the organic materials mixtures such as stalk, plant leaves, industrial refuse, medical waste, domestic refuse.
Accompanying drawing explanation
Fig. 1 is principle of work schematic block diagram of the present invention.Fig. 2 is elementary carbonization gas washing tower, and Fig. 3 is secondary carbonization gas washing tower, and Fig. 4 is self-cleaning interchanger, and Fig. 5 is vapourizing furnace.
In Fig. 2, Fig. 3,3 recirculated water water-ins, 4 recirculated water distributor disks, 5 recirculated water spray lines, 6 carbonization gas entrances, 7 Venturi meters, 8 large Venturi meters, 9 carbonization gas outlets, 10 phlegma tar overflow ports, 11 flashback tanks, 12, phlegma water seal cylinder, 13 tower trays, 14 phlegma liquid discharge pipes, 15 cleanout openings.
In the self-cleaning interchanger of Fig. 4,29 gas compartments, 30 gas converting heat pipes, 31 gas inlet strainers, 32 gas inlet pipes, 33 clean gas outlets, 34 weak base desulfurizing scrubbers, 35 phlegma relief outlets, 36 Wens flutter day with fog, 37 self-cleaning uniform dividers, 38 cleanings go back stomodaeum, 39 upper gas heat exchange tower trays, 40 central gas heat exchange tower trays, 41 lower gas heat exchange tower trays, in 42, tube side connects end socket, 43 recirculated water interfaces.
In Fig. 5 vapourizing furnace, 1 top feed bin, 2 automatic feeding devices, 16 materials enter stove distribution passage, 17 carbonizing gas collect the extraction mouth of pipe and gas diffuses combustion chamber, combustion air left and right dividing plate, 24 automatic discharging devices, 25 air-breathing burning craters, 26 combustion chamber down cycles water jackets, 27 furnace bottom support platforms, 28 nesting box in interface, 18 uniform distributors and gas collection device, 19 bodies of heater, 20 organic materials oxidations, destructive distillation, kiln, 21 combustion air inlet mouths, 22 combustion air even preheating cloth air chamber, 23 stoves.
Embodiment
Accompanying drawing is a kind of specific embodiment of the present invention.
Organic materials integrated conduct method of the present invention, comprises the following steps:
A. the elementary screening of material, removes a small amount of heavy seeds based on metal, and then light material carries out fragmentation pulverizing;
B. mixing of materials forming processes;
C. material enters organic materials carbonization gasified boiler and carries out destructive distillation, discharges half smokeless fuel product and carbonizing gas after material destructive distillation;
D. carbonizing gas carries out elementary washing, purifying through elementary carbonization gas washing tower, removes dust, mink cell focus; Then carry out secondary washing purification through secondary carbonization gas washing tower, remove lightweight oil;
E. after washing, gas carries out elementary de-oiling, dehydration, desulfurization, de-naphthalene, cooling through self-cleaning interchanger, then through another self-cleaning interchanger de-oiling again, dehydration, desulfurization, de-naphthalene, cooling process, the carbonizing gas that clean combustiblecomponents is methane, carbon monoxide, hydrogen is obtained.Specifically, after washing, gas carries out elementary de-oiling, dehydration, cooling through self-cleaning interchanger, and the lightweight oil that self-cleaning system produces and weakly alkaline liquid carry out desulfurization, de-naphthalene to gas.
Organic materials integrated conduct method of the present invention, also comprises step F: the condensation mixed solution after elementary washing is clean enters condensate circulation pond, through settlement separate go out dust, tar.The water being separated rear natural subsidence reenters elementary carbonization gas washing tower and carries out wash cooling to gas, recycles.Gas after initial wash continues to enter secondary carbonization gas washing tower, self-cleaning interchanger, the recirculated water lower by temperature again washs gas, lowers the temperature, phlegma after washing flows into circulation settling bowl, settlement separate de-oiling again, imurity-removal process, the water after precipitate and separate enters systemic circulation and uses.Tar timing after sedimentation is drawn to outside oil tank sells.
In steps A, use strip-type screen screens out a small amount of heavy seeds based on metal, then light material fragmentation is crushed to less than 8 millimeters.
In step B, with forming machine, comminuting matter is prepared into the material of 10-100 millimeter.
In step C, in carbonizing gas, combustiblecomponents is methane, carbon monoxide, hydrogen.
In step F, circulating water temperature goes out tar at 40-60 DEG C of precipitated and separated, thus tar extraction is separated.
Organic materials total system of the present invention, comprises the Supplying Sieving Mechanism, material crushing device, material forming device, organic materials carbonization gasified boiler, elementary carbonization gas washing tower, secondary carbonization gas washing tower, the self-cleaning interchanger that set gradually.
Self-cleaning interchanger comprises the square tube shape gas compartment 29 of above-below direction, the gas converting heat pipe 30 of a large amount of transverse directions is provided with in gas compartment, recirculated cooling water is had in gas converting heat pipe, be provided with gas inlet strainer 31 bottom gas compartment and connect gas inlet pipe 32, gas compartment top has clean gas to export 33 and weak base desulfurizing scrubber 34, and phlegma relief outlet 35 is positioned at bottom gas compartment; Gas converting heat pipe top is also provided with Wen and flutters day with fog 36 and self-cleaning uniform divider 37, is provided with for uniform gas in gas converting heat pipe heat exchange tower tray 39,40,41.Clean gas outlet 33, Wen flutter day with fog 36, weak base desulfurizing scrubber 34, and self-cleaning uniform divider 37, heat exchange tower tray 39,40,41 are arranged in order from top to bottom.self-cleaning interchanger can do de-oiling, dehydration, desulfurization, de-naphthalene, cooling process for carbonizing gas.See Fig. 4.
The nesting box 28 that Organic material gasification furnace comprises body of heater, is arranged on the top feed bin 1 at body of heater top, bottom of furnace body correspondence is arranged; In body of heater, bottom is provided with the organic materials oxidation of several above-below directions side by side, destructive distillation, kiln 20, each organic materials oxidation, destructive distillation, kiln lower end are provided with automatic discharging device 24, are provided with combustion air inlet mouth 21 between adjacent two organic materials oxidations, destructive distillation, kiln; Body of heater internal upper part is provided with carbonizing gas and collects and draw the mouth of pipe and gas and diffuse uniform distributor and gas collection device 18 in interface 17, vapourizing furnace; The wall of organic materials oxidation, destructive distillation, kiln is provided with combustion chamber down cycles water jacket 26.The composition of carbonizing gas comprises methane, hydrogen, carbon monoxide, carbonic acid gas, nitrogen.See Fig. 5.
Elementary carbonization gas washing tower of the present invention, comprise carbonization gas entrance 6 and carbonization gas outlet 9, top is provided with recirculated water spray line 5, and middle part is provided with Venturi meter 7 and large Venturi meter 8, and bottom is provided with flashback tank 11.Flashback tank is provided with phlegma tar overflow port 10.Recirculated water spray line 5 top is provided with recirculated water distributor disk 4, and recirculated water distributor disk is provided with recirculated water water-in 3.Elementary carbonization gas washing tower can remove most of dust, mink cell focus in carbonizing gas.See Fig. 2.
Secondary carbonization gas washing tower of the present invention, comprise carbonization gas entrance 6 and carbonization gas outlet 9, be provided with the tower tray 13 of a large amount of transverse directions in tower body from top to bottom, gas upwards flows from the gap between tower tray, be provided with recirculated water spray line 5 in the middle part of tower body, bottom tower body, be provided with phlegma liquid discharge pipe 14.Cleanout opening 15 is had bottom tower body.Phlegma liquid discharge pipe connects phlegma water seal cylinder 12, and phlegma water seal cylinder is provided with phlegma tar spillway 10.Secondary carbonization gas washing tower can remove the lightweight oil in carbonizing gas and be unfavorable for the portion gas of burning.See Fig. 3.
From self-cleaning interchanger clean gas out, may be used for combustion gas internal combustion generator group, electric power exports supply electricity usage unit, the high-temp waste gas that combustion gas internal combustion generator group produces may be used for generating waste-heat steam boiler system, hot water or steam export hot-water supply and steam applying unit, and hot water and steam applying unit boiler soften condensate water circulatory and input generating waste-heat steam boiler system again.
Vapourizing furnace working process: material enters in vapourizing furnace continuously, run into the high temperature hot gas risen by bottom and carry out reverse exchange, the moisture that removing material outside is carried, material continues descendingly to enter organic materials oxidation, destructive distillation, kiln 7 carry out drying, descendingly again carry out material destructive distillation, remove organic substance in material--carbonizing gas, then continue descending, enter oxidizing fire and destructive distillation thermal source is provided, discharged by bottom roller automatic discharging device 11 afterwards, the solid matter of discharging is half smokeless fuel product, completes retort process.This device produces high-temperature hot gas by air-breathing organic waste materials to carry out destructive distillation to material.
Self-cleaning interchanger is applicable in middle low temperature and high temperature carbonization gas, ultimate purification and cooling, as coordinated other equipment use, the content of objectionable impurities in purified gas (tar, sulfide, oxynitride) can be made to be up to state standards following, in gas, water content is extremely low, free from dust, cleaning gas degree is high.Key points in design is, can according to the temperature of various carbonizing gas, volume density, select different design datas, make the temperature of access arrangement gas from about 100C °, remove water, oil, sulphur, how, after dust and part oxynitride, the temperature of clean carbonization gas is down within 30C °, uses calorific value to play a role to raising carbonization gas.
After self-cleaning interchanger uses the carbonization gas of about scavenging process: 100C ° temperature to enter this equipment, first by carbonization gas inlet filter by carbonization gas extremely trace solid impurity carry out adsorption filtration, carbonization gas is about to part lightweight oil on continuing and is adsorbed on heat transfer tube, continue rising by bottom gas heat exchange tower tray carbonization gas and enter another temperature province continuation heat exchange, mink cell focus is removed substantially in this region, continue up continuation heat exchange by central gas heat exchange tower tray carbonization gas lightweight oil is separated from carbonization gas, continue to go upward to low-temperature region by upper gas heat exchange tower tray, the low-temperature alkali liquid flowed down with top weak base desulfurizing scrubber carries out reverse heat-exchange, make sulphur and weak base source close contact in carbonization gas, remove a small amount of sulphur residual in carbonization gas, these condensed fluids carry out continual self-cleaningly to wash away to device interior from top to bottom, not only remove water in carbonization gas, oil, sulphur, how, dust and part oxynitride, and the tar of condensation adsorption on carbonization gas heat transfer tube and all the other impurity are washed away, finally the solid impurity that carbonization gas inlet filter adheres to also is washed away, phlegma relief outlet finally by device bottom flows out and enters condensate circulation pond.The clean destructive distillation gas port of its upper side discharges clean carbonization gas for generating and other gas equipments.

Claims (7)

1. an organic materials total system, is characterized in that: comprise the Supplying Sieving Mechanism, material crushing device, material forming device, organic materials carbonization gasified boiler, elementary carbonization gas washing tower, secondary carbonization gas washing tower, the self-cleaning interchanger that set gradually;
Elementary carbonization gas washing tower, comprise carbonization gas entrance and carbonization gas outlet, top is provided with recirculated water spray line, and middle part is provided with Venturi meter and large Venturi meter, and bottom is provided with flashback tank; Flashback tank is provided with phlegma tar overflow port;
Secondary carbonization gas washing tower, comprise carbonization gas entrance and carbonization gas outlet, be provided with the tower tray of a large amount of transverse directions in tower body from top to bottom, gas flows from the gap between tower tray, is provided with recirculated water spray line in the middle part of tower body, is provided with phlegma liquid discharge pipe bottom tower body;
Self-cleaning interchanger comprises the square tube shape gas compartment of above-below direction, the gas converting heat pipe of a large amount of transverse directions is provided with in gas compartment, recirculated cooling water is had in gas converting heat pipe, be provided with gas inlet strainer bottom gas compartment and connect gas inlet pipe, gas compartment top has clean gas to export and weak base desulfurizing scrubber, and phlegma relief outlet is positioned at bottom gas compartment; Gas converting heat pipe top is also provided with Wen and flutters day with fog and self-cleaning uniform divider, is provided with several heat exchange tower trays for uniform carbonization gas in gas converting heat pipe; Clean gas exports, Wen flutters day with fog, weak base desulfurizing scrubber, self-cleaning uniform divider, heat exchange tower tray are arranged in order from top to bottom;
The nesting box that Organic material gasification furnace comprises body of heater, is arranged on the top feed bin at body of heater top, bottom of furnace body correspondence is arranged; In body of heater, bottom is provided with the organic materials oxidation of several above-below directions side by side, destructive distillation, kiln, each organic materials oxidation, destructive distillation, kiln lower end are provided with automatic discharging device, are provided with combustion air inlet mouth between adjacent two organic materials oxidations, destructive distillation, kiln.
2. organic materials total system according to claim 1, is characterized in that: the body of heater internal upper part of Organic material gasification furnace is provided with carbonizing gas and collects and draw the mouth of pipe and gas diffuses uniform distributor and gas collection device in interface, vapourizing furnace; The wall of organic materials oxidation, destructive distillation, kiln is provided with combustion chamber down cycles water jacket.
3., by a method for organic materials total system process organic materials according to claim 1, it is characterized in that: comprise the following steps:
A. the elementary screening of material, removes a small amount of heavy seeds based on metal, and then light material carries out fragmentation pulverizing;
B. mixing of materials forming processes;
C. material enters organic materials carbonization gasified boiler and carries out destructive distillation, discharges half smokeless fuel product and carbonizing gas;
D. carbonizing gas carries out elementary washing, purifying through elementary carbonization gas washing tower, removes dust, mink cell focus; Then carry out secondary washing purification through secondary carbonization gas washing tower, remove lightweight oil;
E. after washing, gas carries out elementary de-oiling, dehydration, desulfurization, de-naphthalene, cooling through self-cleaning interchanger, then through another self-cleaning interchanger de-oiling again, dehydration, desulfurization, de-naphthalene, cooling process, obtains the clean carbonizing gas based on methane.
4. organic materials integrated conduct method according to claim 3, it is characterized in that: also comprise step F: the condensation mixed solution after elementary washing, purifying enters condensate circulation pond, through settlement separate go out dust, tar, the water being separated rear natural subsidence reenters elementary carbonization gas washing tower and carries out wash cooling to gas, recycles; Gas after initial wash continues to enter secondary carbonization gas washing tower, self-cleaning interchanger, the recirculated water lower by temperature again washs gas, lowers the temperature, phlegma after washing flows into circulation settling bowl, settlement separate de-oiling again, imurity-removal process, the water after precipitate and separate enters systemic circulation and uses; Tar timing after sedimentation is drawn to outside oil tank sells.
5. organic materials integrated conduct method according to claim 3, is characterized in that: in steps A, and use strip-type screen screens out a small amount of heavy seeds based on metal, then light material fragmentation is crushed within 8 millimeters.
6. organic materials integrated conduct method according to claim 3, is characterized in that: in step B, with forming machine, comminuting matter is prepared into the material of 10-100 millimeter.
7. organic materials integrated conduct method according to claim 3, is characterized in that: in step C, and in carbonizing gas, combustiblecomponents is methane, carbon monoxide, hydrogen.
CN201210573421.4A 2012-12-26 2012-12-26 A kind of organic materials total system and treatment process Active CN103897713B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201210573421.4A CN103897713B (en) 2012-12-26 2012-12-26 A kind of organic materials total system and treatment process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201210573421.4A CN103897713B (en) 2012-12-26 2012-12-26 A kind of organic materials total system and treatment process

Publications (2)

Publication Number Publication Date
CN103897713A CN103897713A (en) 2014-07-02
CN103897713B true CN103897713B (en) 2015-12-23

Family

ID=50989298

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201210573421.4A Active CN103897713B (en) 2012-12-26 2012-12-26 A kind of organic materials total system and treatment process

Country Status (1)

Country Link
CN (1) CN103897713B (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014198075A1 (en) * 2013-06-09 2014-12-18 山东汉菱电气有限公司 System and method for organic material treatment
CN104531216A (en) * 2015-01-06 2015-04-22 梁佩贤 Biomass gas electricity generation and combined heat and electricity supply technology
CN105234158B (en) * 2015-11-13 2016-06-01 岩固(上海)环保科技有限公司 The method of a kind of carbonization gasification hydrogenating reduction process heavy metal ion solid waste
CN110639931A (en) * 2019-09-23 2020-01-03 四川雷鸣环保装备有限公司 Process for coupling kitchen waste and biomass to coproduce oil, electricity, steam and carbon
CN111495924A (en) * 2020-04-10 2020-08-07 漳州微水环保科技有限公司 Resource utilization process for carbonization harmless treatment of biological pharmaceutical residue anoxic gas
CN113546946A (en) * 2021-07-23 2021-10-26 浙江中蓝环境科技有限公司 Anaerobic dry distillation treatment method for medical waste

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101608137A (en) * 2008-06-20 2009-12-23 上海宝钢化工有限公司 Primary cooling process for coal gas
CN101817012A (en) * 2009-02-27 2010-09-01 上海神工环保股份有限公司 Gasification treatment device for household refuse
CN101982528A (en) * 2010-11-23 2011-03-02 神华集团有限责任公司 Gasification device for classified gasification of moving bed, method for gasifying coal and applications thereof
CN201971798U (en) * 2010-11-23 2011-09-14 神华集团有限责任公司 Gasifying device for graded gasification moving bed
CN102719289A (en) * 2012-06-21 2012-10-10 新地能源工程技术有限公司 Process for preparing liquefied natural gas (LNG) and hydrogen from coke oven gas
CN203128495U (en) * 2012-12-26 2013-08-14 山东汉菱电气有限公司 Organic material comprehensive processing system

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201077830Y (en) * 2007-03-23 2008-06-25 周泽宇 Biomass heat pyrolytic air dust removing-washing-selective evaporation-decoking purifying-storage facility

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101608137A (en) * 2008-06-20 2009-12-23 上海宝钢化工有限公司 Primary cooling process for coal gas
CN101817012A (en) * 2009-02-27 2010-09-01 上海神工环保股份有限公司 Gasification treatment device for household refuse
CN101982528A (en) * 2010-11-23 2011-03-02 神华集团有限责任公司 Gasification device for classified gasification of moving bed, method for gasifying coal and applications thereof
CN201971798U (en) * 2010-11-23 2011-09-14 神华集团有限责任公司 Gasifying device for graded gasification moving bed
CN102719289A (en) * 2012-06-21 2012-10-10 新地能源工程技术有限公司 Process for preparing liquefied natural gas (LNG) and hydrogen from coke oven gas
CN203128495U (en) * 2012-12-26 2013-08-14 山东汉菱电气有限公司 Organic material comprehensive processing system

Also Published As

Publication number Publication date
CN103897713A (en) 2014-07-02

Similar Documents

Publication Publication Date Title
CN103897713B (en) A kind of organic materials total system and treatment process
CN104232121B (en) Organic materials carbonization decomposition gasification furnace and organic materials processing method
CN205261566U (en) Solid organic waste resource is made up and is put
CN203128495U (en) Organic material comprehensive processing system
CN103666505B (en) A kind of house refuse or the equipment of organic waste minimizing and energy
CN104229797A (en) Pyrolysis-activation-combustion-gasification integrated furnace, garbage landfill coordinating treatment system and activated carbon preparation method
CN103881738B (en) Organic materials treatment system
CN205261567U (en) Waste gasification boiler
CN104479742A (en) Biomass fuel preparation system
CN105444180B (en) A kind of refuse gasification boiler and its application process
KR101527931B1 (en) The combined heat and power system using a biomass gasification
CN204369820U (en) Biomass gasifying furnace waste heat comprehensive utilization system
CN204369819U (en) From preheating biomass gasifying furnace
CN203451476U (en) Organic material dry distillation and cracking gasifier
CN201890871U (en) Biomass static bed gasification power generation system
TW201437352A (en) Tar-self-removal biological fixed bed gasifier system
CN210085380U (en) Carbon emission reduction system of thermal power plant
CN203672156U (en) Tail gas utilization system for carbonization furnace
CN106477848A (en) The system and method that a kind of recycling sludge is processed
CN102936509B (en) External heat radiation type dry distillation system for oil shale
CN210826083U (en) Fixed bed intermittent type gas making peculiar smell eliminating device
CN206408079U (en) A kind of system of recycling sludge processing
CN204958813U (en) Apparatus for producing of living beings charcoal and pyrolkigneous liquid
CN204689953U (en) A kind of downdraft gasifying biomass station of clean fuel gas
CN204689952U (en) A kind of automatic removing dust downdraft gasifying biomass station

Legal Events

Date Code Title Description
PB01 Publication
C06 Publication
SE01 Entry into force of request for substantive examination
C10 Entry into substantive examination
GR01 Patent grant
C14 Grant of patent or utility model