CN103316890B - Living beings negative pressure degradation pretreatment device - Google Patents
Living beings negative pressure degradation pretreatment device Download PDFInfo
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- CN103316890B CN103316890B CN201310220653.6A CN201310220653A CN103316890B CN 103316890 B CN103316890 B CN 103316890B CN 201310220653 A CN201310220653 A CN 201310220653A CN 103316890 B CN103316890 B CN 103316890B
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- circulating pump
- drainer
- degraded still
- living beings
- negative pressure
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Abstract
A kind of living beings negative pressure degradation pretreatment device, comprises degraded still, fuel manipulator crane structure, pneumatic operated valve, drainer, circulating pump, valve, electric automatic control device, vavuum pump, fan water tank, support hinged, rotary actuation, the strong point, upset drives and heat exchanger, it is characterized in that described degraded still is installed on bloster hinge and connects, support and be hingedly installed on the strong point, the strong point is installed on ground, the built-in heat(ing) coil in degraded still one end is connected with heat exchanger with the first circulating pump in turn, the other end is provided with fuel manipulator crane structure, this fuel manipulator crane structure and degraded still are connected with drainer by pneumatic operated valve, also be connected with drainer with the 3rd circulating pump by valve, described drainer is connected with vavuum pump by valve, be connected with fan water tank by the second circulating pump, described electric automatic control device respectively with fuel manipulator crane structure, first circulating pump, 3rd circulating pump, second circulating pump, pneumatic operated valve, fan water tank, vavuum pump is connected with rotary actuation cable and controls.The present invention have control accurately, automaticity high, extensively apply in living beings negative pressure degradation pretreating process.
Description
Technical field:
The present invention relates to living beings pre-processing device, particularly a kind of living beings negative pressure degradation pretreatment device.
Background technology
Traditional living beings preconditioning technique equipment, its structure is motor-driven rotatable shaft, rotating shaft is provided with the similar structures such as blade or hammer leaf, only with similar components such as the blade be installed in motor-driven rotatable shaft or hammer leaves, the break process such as pressure rolling, shearing, impact are carried out to material, the living beings preconditioning technique equipment of this structure, although for the pretreatment of living beings and exploitation have played effect, but there is following shortcoming and defect: 1. mechanical processing method does not change or destroys living beings internal structure, and biomass conversion utilization rate is very low simultaneously; 2. treatment effeciency is low, and energy consumption is large; 3. hand labor intensity is large, and mechanization degree is low; 4. equipment running noises is large, and dust is many, poor working environment; 5. equipment attrition is fast, and maintenance operation cost is high.
Summary of the invention
The object of this invention is to provide a kind of living beings negative pressure degradation pretreatment device, can efficiently, safety, environmental protection mechanization, industrialization pretreatment are carried out to living beings, improve biomass economy rate, shorten the biomass economy cycle, effectively overcome and avoid the shortcoming that exists in above-mentioned prior art or deficiency.
Living beings negative pressure degradation pretreatment device of the present invention, comprises degraded still, fuel manipulator crane structure, pneumatic operated valve, drainer, circulating pump, valve, electric automatic control device, vavuum pump, fan water tank, supports hinged, rotary actuation, the strong point, upset driving and heat exchanger.Described degraded still is installed on bloster hinge and connects, support and be hingedly installed on the strong point, the strong point is installed on ground, the built-in heat(ing) coil in degraded still one end is connected with heat exchanger with the first circulating pump in turn, the other end is provided with fuel manipulator crane structure, this fuel manipulator crane structure and degraded still are connected with drainer by pneumatic operated valve, also be connected with drainer with the 3rd circulating pump by valve, described drainer is connected with vavuum pump by valve, be connected with fan water tank by the second circulating pump, described electric automatic control device respectively with fuel manipulator crane structure, first circulating pump, 3rd circulating pump, second circulating pump 52, pneumatic operated valve, fan water tank, vavuum pump is connected with rotary actuation cable and controls.
Wherein, in the middle part of described degraded still end cap and fuel manipulator crane structure be connected with drainer by pneumatic operated valve by jet chimney, drainer to be connected with degraded still by circulating pump and valve and by the environment that is evacuated in degraded still.Establish heat(ing) coil in described degraded still, its entrance point is connected with heat exchanger, and its port of export is connected with heat exchanger by the first circulating pump.Be provided with heat exchange coil in described drainer, its port of export is connected with fan water tank by circulating pump, and its entrance point is directly connected with fan water tank.Drainer is connected with degraded still with valve by circulating pump.The output shaft of described rotary actuation is connected with degraded still, and degraded still connects at bloster hinge and rotates around own axes under the driving of rotary actuation.Under described bloster hinge is connected on the driving of upset driving, degraded still does the flip-flop movement of 60 °, left and right around the strong point.Described electrical automatic control equipment drives with upset with fuel manipulator crane structure, circulating pump, pneumatic operated valve, fan water tank, vavuum pump, rotary actuation respectively and is connected.
The present invention compared with prior art tool has the following advantages:
1, reasonable in design, treatment facility floor space is little;
2, the living beings after process, the plastics especially in house refuse melt place unites, and is easy to the sifting sort of subsequent handling;
3, accurate control degradation temperature, pressure and other parameters, guarantee degradation effect, also ensure the safety work of degradation process;
4, to the cooled liquid condensation water of the degraded still with uniform temperature, be back to degraded still, not only save the water consumption of degradation process, and save degraded still intensification energy consumption;
5, in running, without appointing to need what chemical addition agent, without any discharge of poisonous waste, environmental protection;
6, after negative pressure degradation, living beings not only internal structure change, and increase operation rate, and shorten and utilize the cycle, and the pretreatment of the peculiar smell that can also carry out disinfection to some special organic wastes, eliminate;
7, mechanization degree is high, feed, vacuumize, heat up, explosion, cooling, high-temperature condensation water reclaim,
The process complete mechanical equalization such as discharging.
Accompanying drawing explanation
Fig. 1 is a kind of example structure schematic diagram of the present invention.
Detailed description of the invention
Consult Fig. 1, a kind of living beings negative pressure degradation pretreatment device, comprise degraded still 1, fuel manipulator crane structure 2, pneumatic operated valve 3, drainer 4, circulating pump 5, valve 6, electric automatic control device 7, vavuum pump 8, fan water tank 9, support hinged 10, rotary actuation 11, the strong point 12, upset driving 13 and heat exchanger 14.Degraded still 1 is installed on and supports on hinged 10, and support hinged 10 and be installed on the strong point 12, the strong point 12 is installed on ground.The built-in heat(ing) coil in degraded still 1 one end is connected with heat exchanger 14 with the first circulating pump 51 in turn, the other end is provided with fuel manipulator crane structure 2, this fuel manipulator crane structure 2 and degraded still 1 are connected with drainer 4 by pneumatic operated valve 3, are also connected with drainer 4 with the 3rd circulating pump 5 by valve 6.Drainer 4 is connected with vavuum pump 8 by valve 6, is connected with fan water tank 9 by second circulating pump 5 on the left side.Electric automatic control device 7 is connected with fuel manipulator crane structure 2, first circulating pump 51, the 3rd circulating pump 5, second circulating pump 52, pneumatic operated valve 3, fan water tank 9, vavuum pump 8 and rotary actuation 11 cable and controls respectively.
In the middle part of degraded still 1 end cap and fuel manipulator crane structure 2 be connected with drainer 4 by pneumatic operated valve 3 by jet chimney, drainer 4 to be connected with still 1 of degrading by circulating pump 5 and valve 6 and by the environment that is evacuated in degraded still 1.Establish heat(ing) coil in degraded still 1, its entrance point is connected with heat exchanger 14, and its port of export is connected with heat exchanger 14 by circulating pump 5.Be provided with heat exchange coil in drainer 4, its port of export is connected with fan water tank 7 by circulating pump 5, and its entrance point is directly connected with fan water tank 9.Drainer 4 is connected with degraded still 1 with valve 6 by circulating pump 5.The output shaft of described rotary actuation 11 is connected with degraded still 1, and degraded still 1 rotates around own axes under the driving of rotary actuation 11 in support hinged 10.Support hinged 10 under the driving of upset driving 13, degraded still 1 does 60 °, left and right around the strong point 12
Flip-flop movement.Electric automatic control device 7 is connected with fuel manipulator crane structure 2, first circulating pump 51, circulating pump 5, second circulating pump 52, pneumatic operated valve 3, fan water tank 9, vavuum pump 8 and rotary actuation 11 cable and controls respectively.
During operation, degraded still 1 is under the driving of rotary actuation 11, around the strong point 12 opening up rotate 60 °, add living beings and a certain proportion of running water simultaneously, then closed the end cover of degraded still 1 by fuel manipulator crane structure 2, the degraded still 1 after sealing, by vavuum pump 8, drainer 4 is pumped into together with degraded still 2 subnormal ambient of gauge pressure-0.04MPa ~-0.09MPa, now, pneumatic operated valve 3 is closed.Degraded still 2 rotates to horizontal level around the strong point 12 under the driving of rotary actuation 14, degraded still 1 is driven to rotate around own axes in support hinged 10 by rotary actuation 11, living beings in degraded still 1 are stirred uniformly, start heat exchanger 8 subsequently, heat energy in heat exchanger 14 is delivered in degraded still 1 by pumping working medium by the first circulating pump 51, make moisture transient evaporation under subnormal ambient, cause biomass cellulose and cell membrane breakage, after the temperature, pressure in degraded still 1 reaches setting value, open pneumatic operated valve 3 and fan water tank 9 simultaneously, by pneumatic operated valve 3, degraded still 1 is communicated with the drainer 4 of low-temperature negative-pressure is instantaneous, realize the blast action to material in degraded still 1, heat in degraded still 1 enters in drainer 4 along with vaporous water steam, the built-in heat exchange coil of drainer 4 is by the second circulating pump 52 and fan water tank 9 heat exchange, high-temperature steam in drainer 4 is cooled to the liquid condensation water of higher temperature.After temperature and pressure reach setting value in degraded still 1, stop cooling.Open degraded still 1 end cover by fuel manipulator crane structure 2, degraded still 1 around the opening down rotation of the strong point 12 60 °, completes discharging under the driving of rotary actuation 11.After normal operation, degraded still 1 can add the condensed water of the higher temperature with 40 DEG C ~ 90 DEG C by circulating pump 5, again to degrade the required energy consumption that heats up with using water wisely and living beings.
Claims (8)
1. a living beings negative pressure degradation pretreatment device, comprises degraded still, fuel manipulator crane structure, pneumatic operated valve, drainer, circulating pump, valve, electric automatic control device, vavuum pump, fan water tank, support hinged, rotary actuation, the strong point, upset drives and heat exchanger, it is characterized in that described degraded still is installed on bloster hinge and connects, support and be hingedly installed on the strong point, the strong point is installed on ground, the built-in heat(ing) coil in degraded still one end is connected with heat exchanger with the first circulating pump in turn, the other end is provided with fuel manipulator crane structure, this fuel manipulator crane structure and degraded still are connected with drainer by pneumatic operated valve, also be connected with drainer with the 3rd circulating pump by valve, described drainer is connected with vavuum pump by valve, be connected with fan water tank by the second circulating pump, described electric automatic control device respectively with fuel manipulator crane structure, first circulating pump, 3rd circulating pump, second circulating pump, pneumatic operated valve, fan water tank, vavuum pump is connected with rotary actuation cable and controls.
2. living beings negative pressure degradation pretreatment device according to claim 1, it is characterized in that in the middle part of described degraded still end cap and fuel manipulator crane structure is connected with drainer by pneumatic operated valve by jet chimney, drainer to be connected with degraded still by circulating pump and valve and by the environment that is evacuated in degraded still.
3. living beings negative pressure degradation pretreatment device according to claim 1, it is characterized in that establishing heat(ing) coil in described degraded still, its entrance point is connected with heat exchanger, and its port of export is connected with heat exchanger by the first circulating pump.
4. living beings negative pressure degradation pretreatment device according to claim 1, it is characterized in that being provided with heat exchange coil in described drainer, its port of export is connected with fan water tank by circulating pump, and its entrance point is directly connected with fan water tank.
5. the living beings negative pressure degradation pretreatment device according to claim 1 or 4, is characterized in that drainer is connected with degraded still with valve by circulating pump.
6. living beings negative pressure degradation pretreatment device according to claim 1, it is characterized in that the output shaft of described rotary actuation is connected with degraded still, degraded still connects at bloster hinge and rotates around own axes under the driving of rotary actuation.
7. living beings negative pressure degradation pretreatment device according to claim 1, under it is characterized in that described bloster hinge is connected on the driving of upset driving, degraded still does the flip-flop movement of 60 °, left and right around the strong point.
8. living beings negative pressure degradation pretreatment device according to claim 1, is characterized in that described electrical automatic control equipment drives with upset with fuel manipulator crane structure, circulating pump, pneumatic operated valve, fan water tank, vavuum pump, rotary actuation respectively and is connected.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310220653.6A CN103316890B (en) | 2013-06-05 | 2013-06-05 | Living beings negative pressure degradation pretreatment device |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201310220653.6A CN103316890B (en) | 2013-06-05 | 2013-06-05 | Living beings negative pressure degradation pretreatment device |
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| CN103316890A CN103316890A (en) | 2013-09-25 |
| CN103316890B true CN103316890B (en) | 2015-07-29 |
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5221357A (en) * | 1979-03-23 | 1993-06-22 | Univ California | Method of treating biomass material |
| CN101348804A (en) * | 2008-09-17 | 2009-01-21 | 北京林业大学 | Method for separating main ingredients of arboret stalk by low-intensity steam explosion |
| CN102071042A (en) * | 2011-01-30 | 2011-05-25 | 福州大学 | Intelligentized continuous quick microwave cracking device for biomass and waste of biomass |
| CN202744415U (en) * | 2012-08-16 | 2013-02-20 | 广州新普利节能环保科技有限公司 | Landfill leachate treatment device |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DK1259466T3 (en) * | 2000-02-17 | 2009-01-05 | Univ Denmark Tech Dtu | Process for the preparation of lignocellulosic material |
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2013
- 2013-06-05 CN CN201310220653.6A patent/CN103316890B/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5221357A (en) * | 1979-03-23 | 1993-06-22 | Univ California | Method of treating biomass material |
| CN101348804A (en) * | 2008-09-17 | 2009-01-21 | 北京林业大学 | Method for separating main ingredients of arboret stalk by low-intensity steam explosion |
| CN102071042A (en) * | 2011-01-30 | 2011-05-25 | 福州大学 | Intelligentized continuous quick microwave cracking device for biomass and waste of biomass |
| CN202744415U (en) * | 2012-08-16 | 2013-02-20 | 广州新普利节能环保科技有限公司 | Landfill leachate treatment device |
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| CN103316890A (en) | 2013-09-25 |
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Granted publication date: 20150729 Termination date: 20160605 |