CN202989087U - Continuous production system of biomass fuel block - Google Patents
Continuous production system of biomass fuel block Download PDFInfo
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- CN202989087U CN202989087U CN 201220653241 CN201220653241U CN202989087U CN 202989087 U CN202989087 U CN 202989087U CN 201220653241 CN201220653241 CN 201220653241 CN 201220653241 U CN201220653241 U CN 201220653241U CN 202989087 U CN202989087 U CN 202989087U
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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
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
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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
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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Abstract
The utility model discloses a continuous production system of a biomass fuel block. The continuous production system is characterized in that the continuous production system sequentially comprises a capture and conveying system, a raw material smashing system, a raw material stoving system, a pressing block shaping system, a shaping fuel cooling air drying system and a weighting and packing system, wherein the capture and conveying system comprises capture equipment and transloading equipment, the raw material smashing system comprises a cutting machine, a hammer mill and a rubbing machine, the raw material stoving system is composed of a hot blast heater, a rotary dryer, an induced draft fan and a cyclone dust remover, the pressing block shaping system is composed of a large dip angle belt conveyor, an auger delivery depiler, a platform and 4-6 block pressing machines, and the shaping fuel cooling air drying system is formed a belt conveyor and a network chain cooling and air drying machine. The continuous production system achieves continuous production of the biomass fuel block and provides an important way for efficiently using biomass energy. Agriculture and forestry waste is made into the biomass fuel block so that environmental pollution is managed and increasing both production and income of the agriculture can be achieved.
Description
Technical field
The utility model relates to the continuous process system of biomass fuel piece.
Background technology
Agriculture and forestry organic waste material, as stalk, chaff skin, shrub branch, withered leaf, tendril, wood chip, cot, wood shavings, sawdust etc., and the residue of food-processing industry discharge, as grouts, vinasse, beet pulp, waste molasses, bagasse, foodstuffs industry waste etc., cause environmental pollution as not processing, be detrimental to health.And its heat content of these agriculture and forestry organic waste materials and combustibility are a kind of raw materials as the Energy production biomass fuel.
Biomass energy has the characteristics such as kind is many, quantity is large, renewable as the fourth-largest Energy resources.But, as a kind of energy form, have the shortcomings such as resource is disperseed, energy density is low, unit weight is little, accumulating is inconvenient, seriously restricted the large-scale application of biomass energy.
Biomass molding fuel is that loose biomass are pressed into the large lumphy structure of density, provides an important approach for efficiently utilizing biomass energy.The biomass briquette clean health, cheap, easy firing, heat temperature raising is faster than coal, and slag is few, easy to clean.Therefore, biomass molding fuel is coal, liquefied gas and the good substitute energy of traditional fuel wood, has wide future develop.China's biomass moulding technical study exploitation starts from the eighties in 20th century, and China's whole year production biomass molding fuel total amount only has more than 20 ten thousand tons.Tracing it to its cause, is mainly to be subjected to the biomass physicochemical characteristic, on impact of moulding etc., has strengthened the industrialization difficulty of biomass molding fuel as raw material water ratio and granularity, and the key parameters such as the shape of some gordian techniquies such as forming mould, length-to-diameter ratio have to be solved; Present production unit only limits to single machine production, also there is no complete continuous producing apparatus.
Summary of the invention
The object of the present invention is to provide a kind of continuous process system of biomass fuel piece, realized that biomass molding fuel collects the industrialization production of packing of product warehouse-in from raw material.
Technical scheme is that a kind of continuous process system of biomass fuel piece is characterized in that: production system comprises: grasping operation system, raw material pulverizing system, raw material stoving system, compound stalk forming system, shaped fuel cooling air-drying system and weighing and packaging system; Wherein:
Above-mentioned grasping operation system comprises capture apparatus and transloading equipment; Capture apparatus is on the lift arm of shovel loader, grasping teeth to be installed; Transloading equipment is the net cage type tray carriage that is dragged by tractor;
Above-mentioned raw material pulverizing system comprises cutting machine, beater grinder and kneading machine; The discharge port of disintegrating apparatus is facing to the rotary conveyor of raw material stoving system; The cut-out selection of dimension 2-4Cm of cutting machine;
Above-mentioned raw material stoving system is comprised of hotblast stove, rotary type rotary drum drying machine, induced draft fan, tornado dust collector; Hotblast stove is connected on the rotary drum drying machine blast inlet, and induced draft fan is connected on the rotary drum drying machine air outlet, and rotary conveyor blanking place is facing to dryer, and the discharge port of rotary drum drying machine is facing to the high angle belt conveyer transfer roller of compound stalk forming system;
Above-mentioned compound stalk forming system is comprised of high angle belt conveyer transfer roller, helical feed depiler, platform, 4-6 platform briquetting press; The helical feed depiler is arranged on platform, and blanking place of high angle belt conveyer transfer roller is facing to helical feed depiler opening for feed, has 4-6 blanking port below the helical feed depiler, and each blanking port faces toward a briquetting press; Briquetting press adopts Horizontal type pressure torus mould type, and the ring mould forms 45 square nibs of 32x32mm discharging at circumference after by 45 combined modules, and pinch roller adopts the excentric shaft form, changes pinch roller and nib gap by adjusting offset, for different materials; The discharge port of briquetting press is facing to the rotary conveyor of shaped fuel cooling air-drying system;
Above-mentioned shaped fuel cooling air-drying system is become with network chain cooling air-drying mechanism by rotary conveyor; Rotary conveyor blanking place is facing to the feed end of network chain cooling air-drying machine; The discharge end material end of network chain cooling air-drying machine is facing to the weighing sack-filling machine of weighing and packaging system;
Above-mentioned weighing and packaging system is made of weighing sack-filling machine, conveying belt and sack closer.
The production process of above-mentioned production system is as follows:
1, with capture apparatus, the biomass material of collecting is grabbed to the net cage type tray carriage of transloading equipment, drag to raw material pulverizing system place by tractor;
2, first by cutting machine, microscler raw material is cut into 2-4Cm, then with beater grinder or kneading machine powder;
3, the rotary conveyor of the direct incoming stock drying system of material after the pulverizing, be transported to the rotary type rotary drum drying machine by rotary conveyor; Material constantly rolls in rotating cylinder and sheds and fully contact the generation heat exchange with the recent hot blast of hotblast stove, moisture and dust are drawn out of from discharge end by induced draft fan, make material water ratio not higher than 20%, the material of being dried is sent into next process after the tornado dust collector dedusting;
4, entered the high angle belt conveyer transfer roller of compound stalk forming system by the material of oven dry dedusting, rise to the helical feed depiler by the high angle belt conveyer transfer roller, the helical feed depiler is distributed to each briquetting press, material heats up rapidly in pressing process, when temperature reaches 70-100 degree centigrade, xylogen begins to soften, and certain viscosity arranged, when reaching 200-300 degree centigrade, be the molten shape of wriggling, make the Mierocrystalline cellulose tight bond, volume of material reduces, density increases, becoming strip discharges continuously from the mould discharging mouth, can become piece by natural fracture after discharge after unsettled certain-length,
5, the fuel brick that fragments into piece is transported on network chain cooling air-drying machine by rotary conveyor, and cooling by the following cooling fan of network chain in the network chain course of conveying, cooling rear intensity further increases, and becomes biomass molding fuel;
6, biomass molding fuel is entered the hopper of weighing sack-filling machine by the discharge end of network chain cooling air-drying machine, then fall into product bag, after reaching packed weight, the hopper door autoshutdown, then controlling bag clamping device unclamps, packing bag falls automatically, stitches bag by sack closer in tape transport, then the finished product warehouse-in.
The utility model has been realized the continuous production of biomass fuel piece, provides an important approach for efficiently utilizing biomass energy.Agriculture and forestry organic waste material is made the biomass fuel piece, namely administered environmental pollution and made again agricultural production and income.
Description of drawings
Fig. 1 is the production system schematic diagram of embodiment.
Fig. 2 is the compound stalk forming system front view of embodiment.
Fig. 3 is the compound stalk forming system vertical view of embodiment.
Marginal data, 1-hay grabbing machine, 2-net cage type tray car, the 3-cutting machine, 4-rotary conveyor, 5-hotblast stove, 6-rotary type rotary drum drying machine, 7-induced draft fan, 8-tornado dust collector, 9-high angle belt conveyer transfer roller, 10-helical feed depiler, 11-platform, the 12-briquetting press, 13-rotary conveyor, 14-network chain cooling air-drying machine, the 15-weighing sack-filling machine, 16-conveying belt, 17-sack closer.
Embodiment
As shown in Figure 2 in Fig. 1, a kind of continuous process system of biomass fuel piece comprises: grasping operation system, raw material pulverizing system, raw material stoving system, compound stalk forming system, shaped fuel cooling air-drying system and weighing and packaging system; Wherein:
Above-mentioned grasping operation system comprises capture apparatus and transloading equipment; Capture apparatus is on the lift arm of shovel loader, grasping teeth to be installed, thereby consists of hay grabbing machine 1; Transloading equipment is the large volume net cage type tray carriage 2 that is dragged by tractor;
The above-mentioned raw material pulverizing turnkey of setting up departments is drawn together cutting machine 3, beater grinder and kneading machine; The discharge port of disintegrating apparatus is facing to the rotary conveyor 4 of raw material stoving system; The cut-out selection of dimension 2-4Cm of cutting machine 3;
Above-mentioned raw material stoving system is comprised of hotblast stove 5, rotary type rotary drum drying machine 6, air inducing 7, tornado dust collector 8; Hotblast stove 5 is connected on rotary drum drying machine 6 blast inlets, and induced draft fan 7 is connected on rotary drum drying machine 6 air outlets, and rotary conveyor 4 blankings place are facing to dryer 6, and the discharge port of rotary drum drying machine 6 is facing to the high angle belt conveyer transfer roller 9 of compound stalk forming system;
Above-mentioned compound stalk forming system as shown in Figure 2 and Figure 3, it is comprised of high angle belt conveyer transfer roller 9, helical feed depiler 10, platform 11,4-6 platform briquetting press 12; Helical feed depiler 10 is arranged on platform 11, and 9 blankings place of high angle belt conveyer transfer roller are facing to helical feed depiler 10 opening for feeds, has 4-6 blanking port below helical feed depiler 10, and each blanking port faces toward a briquetting press 12; Briquetting press 12 adopts Horizontal type pressure torus mould types, and the ring mould forms 45 square nibs of 32x32mm discharging at circumference after by 45 combined modules, and pinch roller adopts the excentric shaft form, changes pinch roller and nib gap by adjusting offset, for different materials; The discharge port of briquetting press 12 is facing to the rotary conveyor 13 of shaped fuel cooling air-drying system;
Above-mentioned shaped fuel cooling air-drying system is made of rotary conveyor 13 and network chain cooling air-drying machine 14; Rotary conveyor 13 blankings place are facing to the feed end of network chain cooling air-drying machine 14; The discharge end material end of network chain cooling air-drying machine 14 is facing to the weighing sack-filling machine 15 of weighing and packaging system;
Above-mentioned weighing and packaging system is made of weighing sack-filling machine 15, conveying belt 16 and sack closer 17.
Claims (1)
1. the continuous process system of a biomass fuel piece, it is characterized in that: production system comprises successively: grasping operation system, raw material pulverizing system, raw material stoving system, compound stalk forming system, shaped fuel cooling air-drying system and weighing and packaging system; Wherein:
Above-mentioned grasping operation system comprises capture apparatus and transloading equipment; Capture apparatus is on the lift arm of shovel loader, grasping teeth to be installed; Transloading equipment is the net cage type tray carriage that is dragged by tractor;
Above-mentioned raw material pulverizing system comprises cutting machine, beater grinder and kneading machine; The discharge port of disintegrating apparatus is facing to the rotary conveyor of raw material stoving system; The cut-out selection of dimension 2-4Cm of cutting machine;
Above-mentioned raw material stoving system is comprised of hotblast stove, rotary type rotary drum drying machine, induced draft fan, tornado dust collector; Hotblast stove is connected on the rotary drum drying machine blast inlet, and induced draft fan is connected on the rotary drum drying machine air outlet, and rotary conveyor blanking place is facing to dryer, and the discharge port of rotary drum drying machine is facing to the high angle belt conveyer transfer roller of compound stalk forming system;
Above-mentioned compound stalk forming system is comprised of high angle belt conveyer transfer roller, helical feed depiler, platform, 4-6 platform briquetting press; The helical feed depiler is arranged on platform, and blanking place of high angle belt conveyer transfer roller is facing to helical feed depiler opening for feed, has 4-6 blanking port below the helical feed depiler, and each blanking port faces toward a briquetting press; Briquetting press adopts Horizontal type pressure torus mould type, and the ring mould forms 45 square nibs of 32x32mm discharging at circumference after by 45 combined modules, and pinch roller adopts the excentric shaft form, changes pinch roller and nib gap by adjusting offset, for different materials; The discharge port of briquetting press is facing to the rotary conveyor of shaped fuel cooling air-drying system;
Above-mentioned shaped fuel cooling air-drying system is become with network chain cooling air-drying mechanism by rotary conveyor; Rotary conveyor blanking place is facing to the feed end of network chain cooling air-drying machine; The discharge end material end of network chain cooling air-drying machine is facing to the weighing sack-filling machine of weighing and packaging system;
Above-mentioned weighing and packaging system is made of weighing sack-filling machine, conveying belt and sack closer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220653241 CN202989087U (en) | 2012-11-15 | 2012-11-15 | Continuous production system of biomass fuel block |
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| Application Number | Priority Date | Filing Date | Title |
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| CN 201220653241 CN202989087U (en) | 2012-11-15 | 2012-11-15 | Continuous production system of biomass fuel block |
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| CN202989087U true CN202989087U (en) | 2013-06-12 |
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| CN 201220653241 Expired - Fee Related CN202989087U (en) | 2012-11-15 | 2012-11-15 | Continuous production system of biomass fuel block |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105423730A (en) * | 2015-11-12 | 2016-03-23 | 深圳市燕化石油有限公司 | Cooling and drying device for biomass briquette fuel and method thereof |
| CN107245360A (en) * | 2017-08-15 | 2017-10-13 | 建水县千原木业有限公司 | A kind of continuous production processes of biomass molding fuel |
| CN113951093A (en) * | 2021-11-22 | 2022-01-21 | 河北闰沃生物技术有限公司 | Biological water-retaining nutrient substrate module and production process and production line thereof |
-
2012
- 2012-11-15 CN CN 201220653241 patent/CN202989087U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105423730A (en) * | 2015-11-12 | 2016-03-23 | 深圳市燕化石油有限公司 | Cooling and drying device for biomass briquette fuel and method thereof |
| CN105423730B (en) * | 2015-11-12 | 2018-01-19 | 深圳市燕化石油有限公司 | A kind of biomass molding fuel cooling and drying device and its method |
| CN107245360A (en) * | 2017-08-15 | 2017-10-13 | 建水县千原木业有限公司 | A kind of continuous production processes of biomass molding fuel |
| CN113951093A (en) * | 2021-11-22 | 2022-01-21 | 河北闰沃生物技术有限公司 | Biological water-retaining nutrient substrate module and production process and production line thereof |
| CN113951093B (en) * | 2021-11-22 | 2022-09-23 | 河北闰沃生物技术有限公司 | Biological water-retention nutrient substrate module and production process and production line thereof |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130612 Termination date: 20131115 |