CN201065397Y - Cracking hydrocarbons fuel generating system by using organic and biomass - Google Patents
Cracking hydrocarbons fuel generating system by using organic and biomass Download PDFInfo
- Publication number
- CN201065397Y CN201065397Y CNU2007200940309U CN200720094030U CN201065397Y CN 201065397 Y CN201065397 Y CN 201065397Y CN U2007200940309 U CNU2007200940309 U CN U2007200940309U CN 200720094030 U CN200720094030 U CN 200720094030U CN 201065397 Y CN201065397 Y CN 201065397Y
- Authority
- CN
- China
- Prior art keywords
- fuel
- gas
- cracking reactor
- caloic
- liquid
- 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.)
- Expired - Fee Related
Links
Images
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The utility model relates to a cracking type hydrocarbon fuel preparation system using organic compounds and biomass, which is characterized in that a cracking reactor is a closed interlayer tank body, and a material stirring device is arranged in the tank body; a thermal mass grinding device is connected with the cracking reactor via a convey mechanism; the combustible gas is separated from the fuel liquid via the cracking reactor; a gas output port is connected with a gas recovery device, or is fed back to a thermal mass heater for supplying heat source; a fuel liquid recovery port is arranged at the bottom of the tank body to collect the prepared hydrocarbon fuel; a fuel discharge port is connected with a fuel separator; the screened quartz sand is returned back to the thermal mass heater for recycle utilization; the solid fuel is discharged and collected via a discharge opening at the bottom of the fuel separator. The utility model makes full use of the advantages of quartz sand of strong solid phase heat transfer and great heat flow intensity; the flash heating of organic materials and biomass and the rapid precipitation of volatile components are realized; the combustible gas can be fed back to the material preheater, and recovered circularly for reclamation by the thermal mass heater. The utility model has the advantages of decreasing the cost of extra gas source.
Description
Technical field
The utility model discloses a kind of cracking organics matter, biomass are produced the hydrocarbon fuel system, belongs to organism, biomass energy transformation technology field.
Background technology
The organism that the utility model relates to comprises: fossil oils such as coal, coal gangue, resinous shale, chemical materialss such as waste or used plastics, rubber, biomass comprise crop material, timber wood chip, grass, etc. agriculture and forestry organic waste material, animal bone skin etc.Organism, biomass through pyrolysis liquefaction technology are the cutting edge technologies of the present research and development of biomass energy in the world.This technology can will be high-grade easy storage, easily transportation with the mode of production of successive technology and batch production based on the Wood Adhesives from Biomass of wood chip the like waste, energy density is high and substituted liquid fluid fuel (bio oil) easy to use, it not only can be directly used in the burning of equipment such as existing boiler and gas turbine, and can make the quality of the quality of liquid fuel by further modification refinement processing near fuel powered by conventional energy such as diesel oil or gasoline, can therefrom extract Chemicals in addition with commercial value.
In the various technologies of organism, biomass through pyrolysis liquefaction, exist multiple different testing apparatus and technological line, to reach the purpose that increases the bio oil productive rate and improve the energy utilization level.As quick cracking, hydrocracking, vacuum cracking, low temperature pyrolyzer, partial combustion cracking etc., produce the most economic method of liquid fuel with being cracked into fast under the normal pressure, the rotation awl biomass through pyrolysis to-oil reactor of the heat of ablation cracking reactor of Britain Aston university, Vortex reactor that NREL proposes and the design of Dutch Fwente university etc. is typically arranged; The equipment scale of described reactor is comparatively huge, and mechanical contact is worn and torn severe and made operation expense also higher simultaneously, therefore will be restricted in mass-producing is used.
The utility model content
The utility model discloses a kind of cracking organics, biomass are produced the hydrocarbon fuel system, has overcome in existing organism, the biomass through pyrolysis liquefaction process that energy utilization rate is not high, energy consumption is big and shortcoming such as not classification of product liquid.
The technical solution adopted in the utility model is: by material-pulverizing device, material preheater, the caloic well heater, cracking reactor, the gas-liquid fractionator, fuel segregation device and corresponding transporting mechanism constitute, wherein, cracking reactor is the interlayer tank body of sealing, interlayer mechanism is connected with gas thermal cycling heating system, the top of cracking reactor is respectively equipped with caloic dog-house and material dog-house, the bottom is provided with fuel discharge outlet, the material whipping appts is installed in it, the caloic shredding unit is connected with the caloic dog-house of cracking reactor by transporting mechanism, the top that the discharge nozzle of scission reaction gas is located at cracking reactor is communicated with the gas-liquid fractionator, inflammable gas and liquid fuel are carried out gas-liquid separation, the gas delivery port of gas-liquid fractionator connects gas concentration unit or feeds back to the caloic well heater provides thermal source, the bottom of gas-liquid fractionator is provided with liquid fuel and reclaims mouth with the hydrocarbon fuel collection of producing, the fuel discharge outlet of cracking reactor bottom connects the fuel segregation device, by screening quartz sand is separated with solid fuel, heat conduction matter turns back to recycle in the caloic well heater once more through the transmission rig of its outlet, and solid fuel is discharged by the discharge port of fuel segregation device bottom and collected.
Transmission rig between described each device of native system adopts closed screw feeder structure for conveying.
Heat conduction matter comprises: quartz sand, silicon carbide, black silicon carbide, aluminium sesquioxide etc.
Native system is with the positively effect that pre-existing reactors equipment is compared: physical construction is simple, making full use of heat conduction matter solid phase conducts heat strong and advantage such as heat flow rate per unit area is big, realize the flash intensification of organism, biomass and separating out fast of fugitive constituent, inflammable gas is fed back to material preheater, caloic well heater carry out recirculation and recycle, thereby reduced the cost of extra source of the gas.
Description of drawings
Fig. 1 is the structural representation of the utility model system;
Fig. 2 is the utility model cracking reactor structural representation.
Embodiment
As shown in Figure 1, constitute the utility model device by material-pulverizing device 2, material preheater 5, caloic well heater 16, cracking reactor 14, gas-liquid fractionator 21, fuel segregation device 26 and corresponding transporting mechanism; Cracking reactor 14 is the interlayer tank body of sealing, with reference to Fig. 2, the inlet pipe 9 of interlayer mechanism is connected with extraneous gas thermal cycling heating system with escape pipe 8, the top of cracking reactor 14 is respectively equipped with caloic dog-house 13 and material dog-house 10, the bottom is provided with fuel discharge outlet 22, and material whipping appts 12 and temperature inductor 11 are installed in it; The preceding termination material travelling belt 1 of caloic shredding unit 2, organic material is sent in the shredding unit 2, pulverize by pair roller disintegrating mechanism 3, send in the material preheater 5 by screw feeder 4, material preheater 5 bottoms are provided with electric heater unit 6 and gas-heating apparatus 7 is heated to 100～200 ℃ with material, deliver to the material dog-house 10 of cracking reactor 14 by transporting mechanism; Being provided with heating unit 19 in the caloic well heater 16 (is selected from caloic: quartz sand or silicon carbide, black silicon carbide, aluminium sesquioxide) is heated to 400～500 ℃, send in the cracking reactor 14 by caloic dog-house 13, seal the anoxybiotic heat scission reaction under the effect of restir device 12, the gaseous matter that generates is sent in the gas-liquid fractionator 21 by the gas comb 15 on cracking reactor 14 tops, become inflammable gas and liquid hydrocarbon fuel by condenser 20 condensation separation, inflammable gas connects gas concentration unit by the gas delivery port of cracking reactor 14 or feeds back to caloic well heater 16 and material preheater 5 provides thermal source, the bottom of gas-liquid fractionator 14 is provided with liquid fuel and reclaims mouth 24 with the hydrocarbon fuel collection of producing, the fuel discharge outlet 22 of cracking reactor 14 bottoms connects fuel segregation device 26, by the two-stage screening quartz sand is separated with solid fuel, quartz sand turns back to recycle in the caloic well heater 16 once more through the transmission rig 23 of its outlet, solid fuel is discharged by the discharge port 28 of fuel segregation device 26 bottoms and is collected, thereby finishes organism, biomass are produced the whole process of hydrocarbon fuel.
Claims (1)
1. cracking organics matter, biomass are produced the hydrocarbon fuel system, it is characterized in that: mainly by material-pulverizing device, material preheater, the caloic well heater, cracking reactor, the gas-liquid fractionator, fuel segregation device and corresponding transporting mechanism constitute, cracking reactor is the interlayer tank body of sealing, interlayer mechanism is connected with gas thermal cycling heating system, the top of cracking reactor is respectively equipped with caloic dog-house and material dog-house, the bottom is provided with fuel discharge outlet, the material whipping appts is installed in it, the caloic shredding unit is connected with the caloic dog-house of cracking reactor by transporting mechanism, the top that the delivery port of scission reaction gas is located at cracking reactor is communicated with the gas-liquid fractionator, inflammable gas and liquid fuel are carried out gas-liquid separation, the gas delivery port of gas-liquid fractionator connects gas concentration unit or feeds back to the caloic well heater provides thermal source, the bottom of gas-liquid fractionator is provided with liquid fuel and reclaims mouth with the hydrocarbon fuel collection of producing, the fuel discharge outlet of cracking reactor bottom connects the fuel segregation device, by screening heat conduction matter is separated with solid fuel, heat conduction matter turns back to recycle in the caloic well heater once more through the transmission rig of its outlet, solid fuel is discharged by the discharge port of fuel segregation device bottom and is collected, and the transmission rig between each device adopts closed screw feeder structure for conveying.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200940309U CN201065397Y (en) | 2007-07-06 | 2007-07-06 | Cracking hydrocarbons fuel generating system by using organic and biomass |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200940309U CN201065397Y (en) | 2007-07-06 | 2007-07-06 | Cracking hydrocarbons fuel generating system by using organic and biomass |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201065397Y true CN201065397Y (en) | 2008-05-28 |
Family
ID=39482569
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007200940309U Expired - Fee Related CN201065397Y (en) | 2007-07-06 | 2007-07-06 | Cracking hydrocarbons fuel generating system by using organic and biomass |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201065397Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104099115A (en) * | 2014-07-24 | 2014-10-15 | 陕西鼓风机集团西安锅炉有限责任公司（西安特种汽车厂） | Destructive distillation testing device and destructive distillation method |
| CN104736676A (en) * | 2012-10-25 | 2015-06-24 | 国际壳牌研究有限公司 | Process for catalytic cracking a pyrolysis oil |
| CN107930182A (en) * | 2017-12-29 | 2018-04-20 | 内蒙古金旭生物科技有限公司 | A kind of active substance of plant extraction element |
-
2007
- 2007-07-06 CN CNU2007200940309U patent/CN201065397Y/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104736676A (en) * | 2012-10-25 | 2015-06-24 | 国际壳牌研究有限公司 | Process for catalytic cracking a pyrolysis oil |
| CN104099115A (en) * | 2014-07-24 | 2014-10-15 | 陕西鼓风机集团西安锅炉有限责任公司（西安特种汽车厂） | Destructive distillation testing device and destructive distillation method |
| CN104099115B (en) * | 2014-07-24 | 2016-05-11 | 陕西鼓风机集团西安锅炉有限责任公司（西安特种汽车厂） | A kind of retort experiment device and method for destructive distillation |
| CN107930182A (en) * | 2017-12-29 | 2018-04-20 | 内蒙古金旭生物科技有限公司 | A kind of active substance of plant extraction element |
| CN107930182B (en) * | 2017-12-29 | 2024-05-24 | 山西鑫旭生物科技有限公司 | Plant active substance extraction element |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101338210B (en) | System for preparing hydrocarbon fuel by cracking organics and biomass | |
| CN101230284B (en) | Delayed coking treatment method for waste plastics and treatment device thereof | |
| CN101775297B (en) | Carbonization and pyrolysis system for organic matters and biomass | |
| CN201473491U (en) | Biomass fast thermal decomposition device | |
| CN102071042B (en) | Intelligentized continuous quick microwave cracking device for biomass and waste of biomass | |
| CN102849676B (en) | High-temperature water vapor pyrolysis-cracking-gasification device and method for solid fuel | |
| TWI404748B (en) | Continuous pyrolysis system and its application | |
| CN101624531A (en) | Device for preparing bio-oil by utilizing biomass spouted fluidized bed through pyrolysis and fractional condensation | |
| CN202576344U (en) | Equipment for extracting oil fuel from sandy oil sludge or/and organic waste | |
| CN102504855A (en) | Device for producing high-quality biological oil by rapidly pyrolyzing biomasses and waste plastics | |
| CN106947509A (en) | The system and method that a kind of plastics pyrolytic gasification prepares oil product | |
| US20160152898A1 (en) | Dry distillation reactor and method for raw material of hydrocarbon with solid heat carrier | |
| CN201065397Y (en) | Cracking hydrocarbons fuel generating system by using organic and biomass | |
| CN102807884A (en) | Method for preparing biological oil and biological char by thermal cracking and liquefying bamboo wood | |
| CN1962818B (en) | Process for preparing bio-oil by using rapid thermal cleavage technology | |
| CN202152330U (en) | Production system by utilizing biomass raw material for making gasoline and diesel directly | |
| CN101775309B (en) | Method for refining from oil sand by using high-temperature gas-cooled reactor and special equipment | |
| CN109337703A (en) | A kind of biomass continous way is catalyzed preparation high-quality oil-gas integrating device online | |
| CN201605246U (en) | Organism and biomass dry distillation, heating and cracking device | |
| CN102304375A (en) | Oil sand/shale fluidized retorting method and system used thereby | |
| CN116477570A (en) | Device and method for preparing hydrogen from household garbage and/or organic matters | |
| AU2011221434A1 (en) | Mechanical pyrolysis in a shear retort | |
| CN201190149Y (en) | Horizontal type system for preparing hydrocarbon fuel from cracking organics and biomass | |
| CN101613613B (en) | Efficient heat energy utilization method used during fast thermal cracking of straw | |
| WO2021012838A1 (en) | Method and apparatus for hydrocracking mineralized refuse pyrolysis oil |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 130021 3/F, TOWER C, NANBO BUILDING, NO.7043, RENMIN AVENUE, CHANGCHUN CITY, JILIN PROVINCE TO: 130022 3/F, TOWER C, NANBO BUILDING, NO.7043, RENMIN AVENUE, CHANGCHUN CITY |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20100517 Address after: 130022 Changchun Renmin Street, No. 7043 South Building C block 3 layer Patentee after: Su Zhong Address before: The people of 130021 cities in Jilin province Changchun Street No. 7043 South Building C block three layer Patentee before: Su Zhong |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080528 Termination date: 20160706 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |