CN208887247U - A kind of material drying system before gasification of biomass - Google Patents

A kind of material drying system before gasification of biomass Download PDF

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Publication number
CN208887247U
CN208887247U CN201820421554.2U CN201820421554U CN208887247U CN 208887247 U CN208887247 U CN 208887247U CN 201820421554 U CN201820421554 U CN 201820421554U CN 208887247 U CN208887247 U CN 208887247U
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China
Prior art keywords
biomass
gasification
evaporator
wind pipe
drying chamber
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CN201820421554.2U
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Chinese (zh)
Inventor
邵帅
王思佳
冯红翠
周华
陈璐
邓尘
杨智勇
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Huatian Engineering and Technology Corp MCC
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Huatian Engineering and Technology Corp MCC
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/129Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/133Renewable energy sources, e.g. sunlight

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  • Drying Of Solid Materials (AREA)

Abstract

This patent provides the material drying system before a kind of gasification of biomass.Including heat pump circulating system and drying chamber, heat pump circulating system includes condenser, compressor, evaporator and expansion valve, and condenser, compressor, evaporator and expansion valve are in turn connected to form circulation loop by pipeline;Condenser is provided with dry and cold intake stack and xeothermic wind pipe;Xeothermic wind pipe is connected to the drying chamber, and drying chamber is provided with damp and hot wind pipe, and the damp and hot wind pipe is connected to the evaporator.The system has the characteristics that dry Energy Efficiency Ratio is high, and the biomass material after predrying facilitates crushing and transmission, while the moisture generated using pre-dryer, reduces the water consumption of entire technique;Meanwhile photovoltaic and wind power generation plant power generation had both can be used in compressor, it is possible to use the power generation that generator provides, to realize energy-efficient purpose.

Description

A kind of material drying system before gasification of biomass
Technical field
The utility model relates to a kind of electricity generation systems, and in particular to the material drying system before a kind of gasification of biomass belongs to In Biomass Energy Utilization field.
Background technique
With the development of economy, countries in the world electricity needs surges.In China, there are the farm-forestry crop of vast area, agriculture The waste of woods crop is a kind of ideal energy.By gasifying electricity generation technology, biomass energy is converted into electric energy, it can Biomass waste material is handled, and electric power can be provided, is had obvious social and economic benefits.But Biomass Gasification & Power Generation technique is multiple It is miscellaneous, and the biomass material humidity come on Scatter Gather is different, inconvenience crushes and transmission.
Summary of the invention
To make up drawbacks described above, a kind of biomass material predry drying system is provided, it is right using reasonable thermal cycle design Biomass material carries out predrying.
In order to achieve the above objectives, the biomass material predrying service system provided includes: heat pump circulating system and drying Tank, heat pump circulating system include condenser, compressor, evaporator and expansion valve, condenser, compressor, evaporator and expansion valve Circulation loop is in turn connected to form by pipeline;Condenser is provided with dry and cold intake stack and xeothermic wind pipe;Xeothermic outlet air Pipeline is connected to drying chamber, and drying chamber is provided with damp and hot wind pipe, and damp and hot wind pipe is connected to evaporator;
Further, further include electricity generation system for powering for compressor, electricity generation system include biomass gasification device, Internal combustion engine, generator, biomass gasification device are connect with drying chamber;Biomass gasification device is connected to internal combustion engine;
Further, biomass gasification device includes with the sequentially connected biomass treatment apparatus of pipeline, gasification furnace, dedusting Device, washer, drier, air-introduced machine and air accumulator;Biomass treatment apparatus is connect with drying chamber;Air accumulator and internal combustion engine connect It connects;
Further, washer discharge outlet is connected to by pipeline with water purifying tank;The water outlet of water purifying tank passes through washing Water pipe and water pump are connect with washer water inlet;The outlet conduit of evaporator is connected to water purifying tank;
Further, further include photovoltaic and wind power generation plant for powering for compressor.
Due to using heat pump cycle structure, air is entered in condenser by dry and cold intake stack, within the condenser It after being heated, is entered in pre-dryer by xeothermic wind pipe, becomes damp-heat air, damp and hot sky after material is dried Gas is entered in evaporator by damp and hot wind pipe, and damp-heat air is absorbed heat by evaporator, and cooling, condensation condenses the water of formation It is sent in water purifying tank by outlet pipe, the drying hot-air after condensation of water, which enters next circulation, does material It is dry.
Post-order process is entered by pre-dried biomass material, to biomass processes, gasification, successively from biomass Processing equipment, gasification furnace, deduster, washer, drier, air-introduced machine, air accumulator are finally burnt in internal combustion engine, internal combustion engine Drive electrical power generators.Compressor power supply mode has electrical power generators and photovoltaic and wind power generation plant.
Using the system, dry Energy Efficiency Ratio is high, and the biomass material after predrying facilitates crushing and transmission, while using in advance The moisture that drier generates, reduces the water consumption of entire technique;Meanwhile compressor is sent out using photovoltaic and wind power generation plant Electricity, it is possible to use generator electricity realizes energy-efficient effect.
Detailed description of the invention
Fig. 1 is 1 schematic diagram of the utility model embodiment
Fig. 2 is 2 schematic diagram of the utility model embodiment
In figure: 1, condenser;2, compressor;3, evaporator;4, expansion valve;5, dry and cold intake stack;6, xeothermic discharge pipe Road;7, pre-dryer;8, damp and hot wind pipe;9, outlet pipe;10, biomass processes and conveying equipment;11, gasification furnace;12, it removes Dirt device;13, washer;14, drier;15, air-introduced machine;16, air accumulator;17, internal combustion engine;18, generator;19, stand-by power supply Route 20, power supply line;21, photovoltaic and wind power generation plant;22, water purifying tank;23, water pump;24, washing pipe.
Specific embodiment
Embodiment 1
The embodiments of the present invention 1 are described in detail with reference to the accompanying drawing.
The utility model is the material drying system before a kind of gasification of biomass, includes condenser 1, compression referring to attached drawing 1 Machine 2, evaporator 3, expansion valve 4, dry and cold intake stack 5, xeothermic wind pipe 6, pre-dryer 7, damp and hot wind pipe 8, water outlet Pipe 9, biomass processes and conveying equipment 10, gasification furnace 11, deduster 12, washer 13, drier 14, air-introduced machine 15, gas storage Tank 16, internal combustion engine 17, generator 18, power supply line 20, photovoltaic and wind power generation plant 21, water purifying tank 22, water pump 23, washing Water pipe 24.
Condenser 1, compressor 2, evaporator 3, expansion valve 4, dry and cold intake stack 5, xeothermic wind pipe 6, pre-dryer 7, damp and hot wind pipe 8 constitutes predry drying system;Biomass processes and conveying equipment 10, gasification furnace 11, deduster 12, washer 13, drier 14, air-introduced machine 15, gas tank 16, internal combustion engine 17, generator 18 constitute gasification power generation system;Outlet pipe 9, Water warfare Pond 22, water pump 23, washing pipe 24 constitute water piping system.
As shown in Figure 1, evaporator 3, compressor 2, condenser 1, expansion valve 4 constitute a heat pump cycle, in evaporator 3 Become gaseous coolant after refrigerant evaporation heat absorption, gaseous coolant is entered in compressor 3 by copper pipe, and compressor 3 is to gaseous coolant Compressed, so that it becomes the gaseous coolant of high temperature and pressure enters in condenser 1, the refrigerant in condenser 1 to extraneous heat release, Reduce portion temperature and pressure.The refrigerant for reducing portion temperature and pressure enters further decrease temperature and pressure in expansion valve 4, then It into evaporation endothermic in evaporator, so recycles, the electricity of compressor 2 is provided by photovoltaic and wind power generation plant 21.
The refrigerant of high temperature and pressure enters heat release in condenser 1, heated the cold sky come in from dry and cold intake stack 5 Gas, the cold air after heating are entered in pre-dryer 7 by xeothermic wind pipe 6, heat to material, take away part water Point, become damp-heat air.Damp-heat air enters in evaporator 3 by damp and hot wind pipe 8, and the refrigerant in evaporator 3 carries out Decalescence, so that damp-heat air is cooling, condensation, the water for condensing formation enters in water purifying tank 22 by 9 outlet pipes.
It is entered in biomass processes and conveying equipment 10 by the biomass material after drying by drier 7, by crushing It after processing, is transported in gasification furnace 11, gasification generates imflammable gas in gasification furnace 11.Imflammable gas successively passes through Deduster 12, washer 13, Dry Absorber 14, remove particulate matter in deduster 12, further purify in washer 13 With remove the substances such as tar removing, in Dry Absorber 14 absorb part tar, also absorb part moisture content, then sucked by air-introduced machine 15 It into air accumulator 16, finally burns in internal combustion engine 17, internal combustion engine 17 drives generator 18 to generate electricity.
Water in water purifying tank 22 is driven into washing pipe 24 by water pump 23, realizes washer 13 to imflammable gas Spray cleaning.
Embodiment 2
The embodiments of the present invention 2 are described in detail with reference to the accompanying drawing
The present embodiment is the improvement to embodiment 1,
See Fig. 2, pick out stand-by power supply route 19 to compressor 2 from generator 18, when photovoltaic and wind power generation plant 21 When generation deficiency is to supply compressor 2, the electricity consumption of the offer of generator 18 is can be used in compressor 2.
The above is only the preferred embodiments of the utility model, and but protection scope of the utility model is not limited thereto, appoint What those skilled in the art within the technical scope disclosed by the utility model, can make change easily in form and details, It should be covered within the scope of the utility model.Therefore, the protection scope of the utility model should be with claim institute circle Subject to fixed protection scope.

Claims (5)

1. the material drying system before a kind of gasification of biomass, it is characterised in that: described including heat pump circulating system and drying chamber Heat pump circulating system includes condenser, compressor, evaporator and expansion valve, and condenser, compressor, evaporator and expansion valve pass through Pipeline is in turn connected to form circulation loop;The condenser is provided with dry and cold intake stack and xeothermic wind pipe;It is described xeothermic Wind pipe is connected to the drying chamber, and the drying chamber is provided with damp and hot wind pipe, the damp and hot wind pipe with it is described Evaporator connection.
2. the material drying system before gasification of biomass as described in claim 1, it is characterised in that: further include for being compression The electricity generation system of machine power supply, the electricity generation system includes biomass gasification device, internal combustion engine, generator, the gasification of biomass Device is connect with the drying chamber;The biomass gasification device is connected to internal combustion engine.
3. the material drying system before gasification of biomass as claimed in claim 2, it is characterised in that: the biogas makeup It sets including with the sequentially connected biomass treatment apparatus of pipeline, gasification furnace, deduster, washer, drier, air-introduced machine and gas storage Tank;The biomass treatment apparatus is connect with drying chamber;The air accumulator is connect with internal combustion engine.
4. the material drying system before gasification of biomass as claimed in claim 3, it is characterised in that: the washer discharge outlet It is connected to by pipeline with water purifying tank;The water outlet of the water purifying tank is connected by washing pipe and water pump and washer water inlet It connects;The outlet conduit of the evaporator is connected to the water purifying tank.
5. the material drying system before gasification of biomass as described in claim 1, it is characterised in that: further include for being compression The photovoltaic and wind power generation plant of machine power supply.
CN201820421554.2U 2018-03-27 2018-03-27 A kind of material drying system before gasification of biomass Active CN208887247U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201820421554.2U CN208887247U (en) 2018-03-27 2018-03-27 A kind of material drying system before gasification of biomass

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201820421554.2U CN208887247U (en) 2018-03-27 2018-03-27 A kind of material drying system before gasification of biomass

Publications (1)

Publication Number Publication Date
CN208887247U true CN208887247U (en) 2019-05-21

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201820421554.2U Active CN208887247U (en) 2018-03-27 2018-03-27 A kind of material drying system before gasification of biomass

Country Status (1)

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CN (1) CN208887247U (en)

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