CN100447219C - Solar energy storage method and device for biomass gasification energy storage - Google Patents
Solar energy storage method and device for biomass gasification energy storage Download PDFInfo
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- CN100447219C CN100447219C CNB200610039744XA CN200610039744A CN100447219C CN 100447219 C CN100447219 C CN 100447219C CN B200610039744X A CNB200610039744X A CN B200610039744XA CN 200610039744 A CN200610039744 A CN 200610039744A CN 100447219 C CN100447219 C CN 100447219C
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- 239000002028 Biomass Substances 0.000 title claims abstract description 51
- 238000002309 gasification Methods 0.000 title claims abstract description 19
- 238000000034 method Methods 0.000 title claims abstract description 14
- 238000004146 energy storage Methods 0.000 title abstract description 8
- 239000003546 flue gas Substances 0.000 claims abstract description 45
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 42
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 39
- 239000007789 gas Substances 0.000 claims abstract description 37
- 238000002485 combustion reaction Methods 0.000 claims abstract description 12
- 238000003860 storage Methods 0.000 claims description 24
- 238000009825 accumulation Methods 0.000 claims description 21
- 238000006243 chemical reaction Methods 0.000 claims description 19
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims description 10
- 238000010438 heat treatment Methods 0.000 claims description 10
- 238000011084 recovery Methods 0.000 claims description 8
- 239000002737 fuel gas Substances 0.000 claims description 7
- 238000010248 power generation Methods 0.000 claims description 7
- 238000001816 cooling Methods 0.000 claims description 5
- 239000007788 liquid Substances 0.000 claims description 5
- 238000004321 preservation Methods 0.000 claims description 5
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims description 4
- KEAYESYHFKHZAL-UHFFFAOYSA-N Sodium Chemical compound [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 4
- 229910052700 potassium Inorganic materials 0.000 claims description 4
- 239000011591 potassium Substances 0.000 claims description 4
- 239000002023 wood Substances 0.000 claims description 4
- 239000002131 composite material Substances 0.000 claims description 3
- 238000005202 decontamination Methods 0.000 claims description 3
- 230000003588 decontaminative effect Effects 0.000 claims description 3
- 238000006722 reduction reaction Methods 0.000 abstract description 2
- 239000000779 smoke Substances 0.000 abstract 1
- 239000002918 waste heat Substances 0.000 abstract 1
- 239000002994 raw material Substances 0.000 description 7
- 239000000567 combustion gas Substances 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000005243 fluidization Methods 0.000 description 3
- 238000005338 heat storage Methods 0.000 description 3
- 238000007599 discharging Methods 0.000 description 2
- 230000008676 import Effects 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- 206010020843 Hyperthermia Diseases 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000007630 basic procedure Methods 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 235000019628 coolness Nutrition 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000036031 hyperthermia Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000012495 reaction gas Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- -1 stalk Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
Images
Classifications
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- 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
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/40—Solar thermal energy, e.g. solar towers
- Y02E10/44—Heat exchange systems
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/133—Renewable energy sources, e.g. sunlight
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- Processing Of Solid Wastes (AREA)
Abstract
The present invention relates to a solar energy storage method and a device for biomass gasification energy storage, which comprises a solar energy collector, a heat exchanger, a combustor, a recovered waste heat exchanger and a heat pipe type gasification furnace, wherein a heat pipe is arranged in the heat pipe gasification furnace of which an outer wall is provided with a smoke gas jacket, a heat absorbing section is arranged in the flue gas jacket, and a heat release section of the heat pipe is arranged in the heat pipe type gasification furnace. Hot water collected by a solar collector is changed into water vapor by the heat exchanger, the water vapor and biomass are delivered into the gasification furnace for reduction reaction, and combustible gas is produced and then enters a gas holder. Under the condition of scant solar energy supply, the combustible gas then enters a combustion chamber for combustion and releases high-temperature flue gas to supply a solar power system, the flue gas released after combustion in the combustion chamber enters the flue gas jacket of the gasification furnace through the heat exchanger and exhausted by a blower fan after cooled by cold water, and the heated cold water is suitable for domestic use. Therefore, solar energy is stored in the gas holder as part of biomass combustible gas and used as accessory power supply, and the present invention is a simple, high efficiency and reliable way for storing energy.
Description
Technical field:
The present invention relates to a kind of solar heat-storing device, be in particular a kind of solar heat storage method and device thereof of gasifying biomass accumulation of energy.
Background technology:
The energy-storage system of solar energy thermal-power-generating is to guarantee the day and night key of steady running of solar power system, good energy-storage system should have three functions: when the solar radiation peak, unnecessary sun power can be saved, use in order to supplying with power generation system night; Should export the deficiency that the accumulative energy remedies solar radiation at the cloudy weather energy-storage system; In continuous rainy weather or season, energy-storage system should be exported the enough additional energy and guarantee power generation system steady running; With regard to present existing solar energy accumulation system also none can satisfy above-mentioned requirements.
Summary of the invention:
Purpose of the present invention, exactly in order to solve the above-mentioned defective of prior art, and a kind of solar heat storage method and the device thereof that conversion of solar energy is become the gasifying biomass accumulation of energy of medium calorific value gas that provides.
Purpose of the present invention can realize by following technical solution:
The method of the solar heat-preservation of gasifying biomass accumulation of energy, it includes the step that solar collector is gathered hot water, is the raw materials of 400 ℃ of-500 ℃ of water vapors as gasifying biomass with 120 ℃ of-250 ℃ of hot water of solar collector collection by the interchanger formation temperature, water vapor and biomass are sent into carry out gasification reaction in the vapourizing furnace, calorific value 17-21MJ/m in the generation
3Inflammable gas, inflammable gas enters gas storage holder after by decontamination procedure, the stored-gas in the gas storage holder enters the combustion chamber under the situation of sun power undersupply, as the supplementary energy of solar electrical energy generation or heat supply; 900 ℃-1000 ℃ the high-temperature flue gas one tunnel that discharges after the combustion chambers burn removes solar power system, the flue gas chuck that another road enters vapourizing furnace by interchanger through 650 ℃ of-700 ℃ of flue gases after the heat exchange after the supercooled water cooling, get rid of by blower fan, the cold water of heating is used for civilian.
The solar heat-storing device of gasifying biomass accumulation of energy, it includes solar collector, the hot water water storage device, interchanger, cleaner, gas storage holder, burner, heat recovery heat exchanger, it also includes the heat pipe-type vapourizing furnace, be provided with heat pipe in it, heat pipe-type vapourizing furnace upper end is provided with the air outlet, the lower end is provided with material inlet, described heat pipe-type vapourizing furnace outer wall is provided with the flue gas chuck, the endotherm section of heat pipe is located in the flue gas chuck, the heat release section of heat pipe is located in the heat pipe-type vapourizing furnace, solar collector is connected with the hot water water storage device, the hot water water storage device is communicated with by in interchanger and the heat pipe-type vapourizing furnace, the combustible gas of heat pipe-type vapourizing furnace (reaction gas) outlet is communicated with gas-holder by strainer, and gas-holder is communicated with burner, and pipeline is leaded up in the outlet side of burner, interchanger is communicated with heat pipe-type vapourizing furnace flue gas chuck outward, another road is connected with power generation system, and pipeline is passed through in the air outlet of heat pipe-type vapourizing furnace flue gas chuck, the air outlet of heat recovery heat exchanger is connected with blower fan.
The purpose of invention also can further realize by following technical measures:
The method of the solar heat-preservation of aforesaid gasifying biomass accumulation of energy, it includes the step that solar collector is gathered hot water, it is 400 ℃ of-500 ℃ of water vapors that 120 ℃ of-250 ℃ of hot water of solar collector collection flue gas heating by biological fuel gas is generated temperature, water vapor and biomass are sent into carry out gasification reaction in the vapourizing furnace, calorific value 17-21MJ/m in the generation
3Inflammable gas, inflammable gas enters gas storage holder after by decontamination procedure, the stored-gas in the gas storage holder enters the combustion chamber under the situation of sun power undersupply, as the supplementary energy of solar electrical energy generation or heat supply; 900 ℃-1000 ℃ the high-temperature flue gas one tunnel that discharges after the combustion chambers burn removes solar power system, the flue gas chuck that another road enters vapourizing furnace by interchanger through 650 ℃ of-700 ℃ of flue gases after the heat exchange after the supercooled water cooling, get rid of by blower fan, the cold water of heating is used for civilian.
The method of the solar heat-preservation of aforesaid gasifying biomass accumulation of energy, wherein said biomass are abandoned biomass such as stalk, wood chip, shell.
The solar heat-storing device of aforesaid gasifying biomass accumulation of energy, the heat transfer tube that is provided with in the wherein said vapourizing furnace are the heat transfer tube of high-temperature heat pipe or spiral pipe or tubulation form.
The solar heat-storing device of aforesaid gasifying biomass accumulation of energy, wherein said high-temperature heat pipe are that sodium Metal 99.5, potassium are the heat pipe of working liquid.
The solar heat-storing device of aforesaid gasifying biomass accumulation of energy, wherein said interchanger are high temperature wave-fin tube heat-exchanger or shell and tube heat exchanger, plate-fin heat exchanger.
The solar heat-storing device of aforesaid gasifying biomass accumulation of energy, the collector of wherein said sun power are tower, slot type or composite parabolic heat collector.
The present invention passes through the raw material of the flue gas heating generation water vapor of biological fuel gas as gasifying biomass with the hot water that solar collector is gathered, in biomass gasifying furnace, react with the biomass generating gasification, the combustion gas of calorific value is stored in the gas holder in the generation, at the overcast and rainy or night that does not have the sun, as the supplementary energy of solar electrical energy generation or heat supply.This unnecessary solar water is become steam, as the raw material of gasifying biomass and biomass (stalk, wood chip, shell etc.) in vapourizing furnace, react obtain in the biological fuel gas of calorific value be stored in gas holder in order to using, also be about to conversion of solar energy and become medium calorific value gas, both being convenient to storage also is convenient to use, and in storing and reusing, there is not extra loss, it not only can satisfy above-mentioned three requirements well, and is that a simple and reliable non-harmful renewable energy source combination utilizes system.
Purpose of the present invention, advantage and characteristics will illustrate by the non-limitative illustration of following preferential embodiment and explain that these embodiment only provide as an example with reference to accompanying drawing.
Description of drawings:
Fig. 1 is a system flow synoptic diagram of the present invention.
Fig. 2 is a high-temperature heat pipe principle of work synoptic diagram of the present invention.
Fig. 3 is a wave-fin tube heat-exchanger structural representation of the present invention.
Fig. 4 is the gasification furnace structure synoptic diagram of another kind of form of the present invention.
Embodiment:
Embodiment one
As shown in Figure 1, the solar heat-storing device of gasifying biomass accumulation of energy of the present invention, it includes solar collector 28, hot water water storage device 23, wave-fin tube heat-exchanger 4, cleaner 9, gas storage holder 6, burner 7, heat recovery heat exchanger 17, the collector 28 of sun power is tower, slot type or composite parabolic heat collector, this device also includes heat pipe-type vapourizing furnace 1, is provided with heat pipe 2 in it, and the heat pipe 2 that is provided with in the described vapourizing furnace 1 is high-temperature heat pipe.Described high-temperature heat pipe 2 is the heat pipe of working liquid for sodium Metal 99.5, potassium.Heat pipe-type vapourizing furnace upper end is provided with air outlet 24, the lower end is provided with material inlet 25, described heat pipe-type vapourizing furnace outer wall is provided with flue gas chuck 3, the endotherm section 26 of heat pipe is located in the flue gas chuck 3, the heat release section 27 of heat pipe is located in the heat pipe-type vapourizing furnace, solar collector 28 is connected with hot water water storage device 23, hot water water storage device 23 is by the wave- fin pipe 5 and 1 interior connection of heat pipe-type vapourizing furnace of interchanger 4, and described interchanger 4 is high temperature wave-fin tube heat-exchanger, shell and tube heat exchanger, plate-fin heat exchanger.The vapour outlet 24 of heat pipe-type vapourizing furnace is communicated with gas-holder 6 by cleaner 9, gas-holder 6 is communicated with burner 7, lead up to the outer flue gas chuck 3 of pipeline, interchanger 4 and heat pipe-type vapourizing furnace and be communicated with in the outlet side of burner 7, another road is connected with power generation system, and the air outlet of flue gas chuck 3 is connected with blower fan 21 by the air outlet of pipeline 16, heat recovery heat exchanger 17.Among Fig. 1, unnecessary hot water (or steam) 10 from the solar energy acquisition system, be heated to 400-500 ℃ raw material as gasifying biomass by the high-temperature flue gas 13 outside the pipe through interchanger 4 in wave-fin pipe 5, enter heat pipe-type vapourizing furnace 1 and carry out gasification reaction with biomass 22, its main reaction is C+H
2O → CO+H
2, this reaction is thermo-negative reaction, and temperature of reaction is between 700-850 ℃, and heat and keeping by high-temperature heat pipe 2 of gasification reaction temperature that reaction absorbs provide.Concrete structure figure sees Fig. 2, the endotherm section 26 of high-temperature heat pipe 2 is in the flue gas chuck 3 of vapourizing furnace among the figure, high-temperature flue gas 12 flows through heat pipe 2, heat is passed to the endotherm section 26 of heat pipe, sodium vaporizing liquid in the inside heat pipe wick absorbs heat that high-temperature flue gas imports into and heat is passed to heat pipe heat release section 27, heat release section 27 is positioned at vapourizing furnace 1, and the heat pipe liberated heat guarantees to keep the vaporization temperature in the vapourizing furnace, and provides gasification reaction required heat.Water vapor 11 and biomass 22 are reacted the middle calorific value (17-21MJ/m that the back generates in vapourizing furnace 1
3) combustible gas 15, through behind the cleaner 9, enter gas storage holder 6 storages.When the sun power undersupply, as at the overcast and rainy or night that does not have the sun, the combustion gas in the gas storage holder 6 enters burner 7, and 8 internal combustion form high-temperature flue gas 14 (900-1000 ℃) in the combustion chamber.High-temperature flue gas 14 can enter solar power system and substitute or additional solar energy, the part 13 of flue gas makes it produce the raw material that high-temperature steam 11 becomes the gasification of vapourizing furnace endogenous substance by the hot water of interchanger 4 heating storage sun power, enter the flue gas chuck 3 of vapourizing furnace through the flue gas 12 (850-900 ℃) of interchanger 4, heat is passed to the endotherm section 26 of heat pipe 2, the flue gas 16 of discharging from flue gas chuck 3 enters heat recovery heat exchanger 17, heating cold water 18 makes it to become hot water 19 for civilian, and the flue gas after interchanger 17 coolings is through blower fan 21 dischargings.
Embodiment two
Fig. 4 is the another kind of structure formation of vapourizing furnace of the present invention.The burner hearth of vapourizing furnace 1 is distributed as 1 and 1 ' two portions.The 1st, the fluidized reaction zone of biomass 22 and water vapor 11,1 ' is the ash fall district of biomass combustible gas 15.Biomass 22 are added by the top of fluidization regions 1, and water vapor 11 enters fluidization regions by the bottom spray orifice 30 of fluidization regions 1 and biomass 22 are reacted.Reacted lime-ash overflows by 29.The lime-ash that the biomass combustible gas 15 that generates is taken out of is in 1 ' negative area sedimentation.Lime-ash screen plate 31 is arranged in the negative area outlet.High-temperature flue gas 13 is passed to heat the endotherm section 26 of high-temperature heat pipe 2 in heating chamber 33.Helical fin 32 is arranged on the endotherm section 26.High-temperature heat pipe 2 reaches the heat pipe heat release section 27 that is positioned at vapourizing furnace reaction zone 1 with the heat of flue gas, and to provide gasifying biomass required reaction heat, the flue gas 16 after the cooling is expelled to heat recovery heat exchanger 17.Present embodiment work basic procedure such as embodiment one are identical, are not giving unnecessary details at this.
Present method includes the step that solar collector is gathered hot water, the hot water that solar collector is gathered passes through the raw material of the flue gas heating generation water vapor of biological fuel gas as gasifying biomass, in biomass gasifying furnace, react with the biomass generating gasification, the combustion gas of calorific value is stored in the gas holder in the generation, not having the sun or night, as the supplementary energy of solar electrical energy generation or heat supply.
Sun power storage mode of the present invention is not only applicable to the large-sized solar power generation system, is suitable for the solar chp system of discrete areas yet, and the exhaust steam water coolant of solar heat power generation system also can be back in the hot water water tank 23.
The present invention produces the raw material (water vapor gasification installation) of hyperthermia and superheating steam as gasifying biomass with unnecessary sun power.With biomass (stalk, wood chip, bark, shell etc.) reduction reaction taking place, generates CO, H in biomass gasifying furnace
2And CH
4, fuel gases calorific value can reach 17-21MJ/m
3, the principal reaction of water vapor gasification is thermo-negative reaction, therefore needs extra thermal source, thermal source imports vapourizing furnace into by the heat of high-temperature heat pipe (is the heat pipe of working liquid with sodium Metal 99.5, potassium) absorption combustion gas flue gas, guarantees normally carrying out of reaction.Sun power is stored in gas holder with regard to a part that becomes biological fuel gas and uses as supplementary energy like this, is a kind of simple and effective and accumulation of energy mode reliably.
In addition to the implementation, the present invention can also have other embodiments.All employings are equal to the technical scheme of replacement or equivalent transformation formation, all drop in the protection domain of requirement of the present invention.
Claims (7)
1. the method for the solar heat-preservation of gasifying biomass accumulation of energy, it includes the step that solar collector is gathered hot water, it is characterized in that: it is 400 ℃ of-500 ℃ of water vapors that 120 ℃ of-250 ℃ of hot water of solar collector collection flue gas heating by biological fuel gas is generated temperature, water vapor and biomass are sent into carry out gasification reaction in the vapourizing furnace, calorific value 17-21MJ/m in the generation
3Inflammable gas, inflammable gas enters gas storage holder after by decontamination procedure, the stored-gas in the gas storage holder enters the combustion chamber under the situation of sun power undersupply, as the supplementary energy of solar electrical energy generation or heat supply; 900 ℃-1000 ℃ the high-temperature flue gas one tunnel that discharges after the combustion chambers burn removes solar power system, the flue gas chuck that another road enters vapourizing furnace by interchanger through 650 ℃ of-700 ℃ of flue gases after the heat exchange after the supercooled water cooling, get rid of by blower fan, the cold water of heating is used for civilian.
2. the method for the solar heat-preservation of gasifying biomass accumulation of energy according to claim 1 is characterized in that: described biomass are stalk, wood chip, shell biomass material.
3. the solar heat-storing device of gasifying biomass accumulation of energy, it includes solar collector, the hot water water storage device, interchanger, cleaner, gas storage holder, burner, heat recovery heat exchanger, it is characterized in that it also includes the heat pipe-type vapourizing furnace, be provided with heat pipe in it, heat pipe-type vapourizing furnace upper end is provided with the air outlet, the lower end is provided with material inlet, described heat pipe-type vapourizing furnace outer wall is provided with the flue gas chuck, the endotherm section of heat pipe is located in the flue gas chuck, the heat release section of heat pipe is located in the heat pipe-type vapourizing furnace, solar collector is connected with the hot water water storage device, the hot water water storage device is communicated with the heat pipe-type vapourizing furnace is interior by the wave-fin pipe of wave-fin tube heat-exchanger, the combustible gas outlet of heat pipe-type vapourizing furnace is communicated with gas-holder by strainer, gas-holder is communicated with burner, pipeline is leaded up in the outlet side of burner, interchanger is communicated with heat pipe-type vapourizing furnace flue gas chuck outward, another road is connected with power generation system, and pipeline is passed through in the air outlet of flue gas chuck, the air outlet of heat recovery heat exchanger is connected with blower fan.
4. the solar heat-storing device of gasifying biomass accumulation of energy according to claim 3 is characterized in that being provided with in the described vapourizing furnace heat transfer tube of high-temperature heat pipe or spiral pipe or tubulation form.
5. the solar heat-storing device of gasifying biomass accumulation of energy according to claim 4 is characterized in that described high-temperature heat pipe is that sodium Metal 99.5 or potassium are the heat pipe of working liquid.
6. the solar heat-storing device of gasifying biomass accumulation of energy according to claim 3 is characterized in that described interchanger is high temperature wave-fin tube heat-exchanger, shell and tube heat exchanger or plate-fin heat exchanger.
7. the solar heat-storing device of gasifying biomass accumulation of energy according to claim 3, the collector that it is characterized in that described sun power are tower, slot type or composite parabolic heat collector.
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| CNB200610039744XA CN100447219C (en) | 2006-04-21 | 2006-04-21 | Solar energy storage method and device for biomass gasification energy storage |
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| CNB200610039744XA CN100447219C (en) | 2006-04-21 | 2006-04-21 | Solar energy storage method and device for biomass gasification energy storage |
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| CN100447219C true CN100447219C (en) | 2008-12-31 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2458529A (en) * | 2008-03-25 | 2009-09-30 | Saigas Ltd | Extracting energy products from biomass using solar energy |
| CN101839225A (en) * | 2010-05-25 | 2010-09-22 | 郑斌 | Biomass-assisted solar generating device |
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| CN101793444B (en) * | 2010-03-08 | 2012-05-30 | 河南农业大学 | Solar energy and biomass energy combined absorption type refrigeration device |
| CN101906996A (en) * | 2010-07-20 | 2010-12-08 | 华北电力大学（保定） | Cogeneration system by firing coil assisted by biomass and solar energy |
| CN101892877A (en) * | 2010-07-20 | 2010-11-24 | 华北电力大学（保定） | Renewable energy resource assistant coal hybrid power generation system |
| CN102080821A (en) * | 2010-11-17 | 2011-06-01 | 华北电力大学（保定） | Heater system for renewable energy auxiliary coal |
| CN102012013A (en) * | 2010-11-17 | 2011-04-13 | 华北电力大学（保定） | Biomass and solar assisted coal fired power plant heater system |
| CN105273761A (en) * | 2014-07-01 | 2016-01-27 | 金广恒环保技术（南京）有限公司 | Organic waste gasification treatment system by utilizing solar energy |
| CN104877709B (en) * | 2015-06-04 | 2017-04-12 | 中国科学院工程热物理研究所 | Solar high-temperature thermochemical gasification reactor |
| CN105485895B (en) * | 2015-12-29 | 2022-07-26 | 广州市祈雅典环保科技有限公司 | Built-in biomass gasification combustion water heater |
| CN108485717B (en) * | 2018-04-23 | 2023-09-26 | 中国石油大学(华东) | All-weather operation solar gasification reactor |
| CN111412775B (en) * | 2020-05-07 | 2024-04-05 | 山东英电环保科技有限公司 | Special high-temperature area heat pipe type heat exchanger for urban and rural waste gasification furnace |
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| CN1085522A (en) * | 1993-10-18 | 1994-04-20 | 李宗英 | Utilize sun power from biomass and water, to produce hydrogen processing method and equipment thereof |
| CN1391074A (en) * | 2002-04-24 | 2003-01-15 | 郑茂余 | Method and equipment for using solar energy to accumulate heat and provide heat or cold |
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2006
- 2006-04-21 CN CNB200610039744XA patent/CN100447219C/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1085522A (en) * | 1993-10-18 | 1994-04-20 | 李宗英 | Utilize sun power from biomass and water, to produce hydrogen processing method and equipment thereof |
| CN1391074A (en) * | 2002-04-24 | 2003-01-15 | 郑茂余 | Method and equipment for using solar energy to accumulate heat and provide heat or cold |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2458529A (en) * | 2008-03-25 | 2009-09-30 | Saigas Ltd | Extracting energy products from biomass using solar energy |
| CN101839225A (en) * | 2010-05-25 | 2010-09-22 | 郑斌 | Biomass-assisted solar generating device |
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| CN1844313A (en) | 2006-10-11 |
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