CN205640917U - Disease animals high temperature degradation back waste liquid waste gas burns device - Google Patents
Disease animals high temperature degradation back waste liquid waste gas burns device Download PDFInfo
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- CN205640917U CN205640917U CN201620446090.1U CN201620446090U CN205640917U CN 205640917 U CN205640917 U CN 205640917U CN 201620446090 U CN201620446090 U CN 201620446090U CN 205640917 U CN205640917 U CN 205640917U
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Abstract
The utility model discloses a disease animals high temperature degradation back waste liquid waste gas burns device, its including the closed breaker that connects gradually, high pressure and high temperature sterilization apparatus, grease separator, fermentation degradation device, waste liquid waste gas burn device, waste heat utilization equipment, heat exchanger, spray absorbing device, fog water separator. This application through heat sterilization, has cooperated oxygen biodegradable to handle disease animals corpse and discarded object in airtight environment, turns into high -quality fertilizer raw materials, and high -quality organic fertilizer can be made in further processing, reaches the sterilization, decrement, environmental protection and resource cyclic utilization's purpose, in addition, this application is burned technology through high temperature and is become harmless material with high concentration waste liquid, the waste gas of cooking, and the atmospheric dilution makes the three wastes discharge the environmental protection standard that reaches the country, does not produce secondary pollution to with the heat recovery who produces among the burning process.
Description
Technical field
This utility model belongs to animals with diseases harmless treatment field, is specifically related to waste liquid burned waste gas device after a kind of animals with diseases high temperature degradation.
Background technology
Animals with diseases harmless treatment, always one difficulties.Buried, deep-well system, traditional processing method such as direct burning of animal, owing to by environmental protection poisonous and harmful substances such as () sewage effluent, flue dust, waste gas, (including bio-safety) safely, the factor impact such as processing cost, it is difficult to wide popularization and application.The most therefore, animals died of illness can not be effectively addressed, and causes epidemic disease to spread, and even animals died of illness comes into the market.
The appearance of high temperature degradation animals with diseases technology, for animal harmless treatment, it is provided that effective technology and the guarantee of means.High temperature degradation desirably prevents animal epidemic and zoonosis is propagated, and protects health；Be conducive to flowing to dining table from Sources controlling Pork form diseased or dead pigs, it is ensured that the people are able to eat quality-assured meat；Be conducive to controlling environmental pollution.
China is pig-breeding big country, and cultivation is the mainstay industry of farmer richness, and high temperature degradation and the application of waste liquid waste gas innoxious burning Technique Popularizing are the most significant to animal husbandry sustainable development and new countryside construction etc..
In closed environment, by high temperature sterilize, aerobic biodegradation is coordinated to process sick pig corpse and garbage, it is converted into and can produce high-quality organic fertilizer raw material, be processed further, can be made into high-quality organic fertilizer, reach the purpose of sterilizing, decrement, environmental protection and resource circulation utilization.
But during high temperature degradation, oily-water seperating equipment can produce high concentration harmful rotten waste liquid, the stench steam produced during steaming and decocting spoil, harmful waste liquid content of organics is high, general sewage disposal cannot process up to standard, when steaming and decocting, generation foul gas directly discharges and affects operator and surrounding, by high temperature incineration technique, high-concentration waste liquid, steaming and decocting waste gas become harmless material, enter air, three waste discharge is made to reach the environmental protection standard of country, do not produce secondary pollution, and the heat recovery that will produce in burning process.
Utility model content
For problems of the prior art, the purpose of this utility model is to provide waste liquid burned waste gas device after a kind of animals with diseases high temperature degradation, this incinerator makes three waste discharge reach the environmental protection standard of country, does not produce secondary pollution, and the heat recovery that will produce in burning process.
For achieving the above object, this utility model is by the following technical solutions:
Waste liquid burned waste gas device after a kind of animals with diseases high temperature degradation, closed crushing device that described incinerator includes being sequentially connected with, high pressure-temperature bactericidal unit, fat separator device, fermentative degradation device, waste liquid burned waste gas device, residual heat using device, heat exchanger, spray-absorption device, mist water separator；Wherein,
Described closed crushing device, for being crushed by the corpse of animals with diseases, crushes and is delivered to described high pressure-temperature bactericidal unit afterwards；
The corpse of described high pressure-temperature bactericidal unit animals with diseases after crushing carries out high temperature sterilize, afterwards waste liquid and oils and fats is delivered to described fat separator device, residue is delivered to described fermentative degradation device；
Described fat separator device is for separating described waste liquid and oils and fats, and isolated oils and fats uses as biodiesel raw material, and isolated waste liquid enters described waste liquid burned waste gas device；
It is organic fertilizer that described fermentative degradation device is used for described residue fermentative degradation；
Described waste liquid burned waste gas device is for being converted into high-temperature flue gas by described waste liquid through high-temp combustion, and described high-temperature flue gas is delivered to described residual heat using device；
Described residual heat using device for carrying out UTILIZATION OF VESIDUAL HEAT IN to described high-temperature flue gas, and the waste heat recycled is delivered to described high pressure-temperature bactericidal unit, and by lowering the temperature, later flue gas is delivered to described heat exchanger；
Described heat exchanger is for carrying out waste heat recycling to later flue gas of lowering the temperature, and the waste heat recycled is delivered to described waste liquid burned waste gas device, waste heat recycles later flue gas and is delivered to described spray-absorption device；
Described spray-absorption device is used for absorbing remaining deleterious acidic gas and little granule dust in removal flue gas；Then flue gas being delivered to described mist water separator, described mist water separator the water in flue gas and gas is separated, the gas after separation is sent into chimney through air-introduced machine and enters atmosphere.
Further, described incinerator also includes that waste liquid stirs storage tank, waste liquid transfer pipeline, Waste liquid atomization jetting device；Described waste liquid stirring storage tank will be for being stirred through the isolated waste liquid of described fat separator device, and inputting described Waste liquid atomization jetting device through described waste liquid transfer pipeline after filtering, the waste liquid after filtration sprays into described waste liquid burned waste gas device after described Waste liquid atomization jetting device is atomized.
Further, described incinerator also includes air compressor and compressed air tunnel；Compressed air is delivered to described Waste liquid atomization jetting device through described compressed air tunnel by described air compressor；For the waste liquid after described Waste liquid atomization jetting device is atomized is sprayed into described waste liquid burned waste gas device.
Further, described incinerator also includes urgent bypass line and absorbent charcoal adsorber, and the waste gas produced in described high pressure-temperature bactericidal unit and fermentative degradation device enters air after described urgent bypass line and absorbent charcoal adsorber.
Further, described incinerator also includes that oxygenating blower fan, described oxygenating blower fan are connected with described heat exchanger.
Further, the inwall that described waste liquid burned waste gas device is cylindrical is lined with the stove of refractory material.
Further, described residual heat using device is waste heat boiler.
Further, described incinerator also includes electric-control system and temperature control system, and described electric-control system is implemented power supply for power-equipment each to waste disposal facilities and automatically controls；Described temperature control system is for being monitored and controlled the temperature in burning process and flame.
Further, being provided with temperature sensor in described waste liquid burned waste gas device, described temperature sensor is connected with described temperature control system, for providing the temperature information in waste liquid burned waste gas device to described temperature control system.
Further, being provided with burner in described waste liquid burned waste gas device, the open and close of described burner are by described electric control system controls；After described burner starts, when making temperature in waste liquid burned waste gas device be promoted to 900-1100 DEG C, burner extinguishes, and when in-furnace temperature drops to 850 DEG C, burner is automatically lighted and again heated, runs so forth.
This utility model has a following Advantageous Effects:
The application is in closed environment, by high temperature sterilize, coordinates aerobic biodegradation to process animals with diseases corpse and garbage, it is converted into high-quality organic fertilizer raw material, is processed further, can be made into high-quality organic fertilizer, reach the purpose of sterilizing, decrement, environmental protection and resource circulation utilization；Additionally, high-concentration waste liquid, steaming and decocting waste gas are become harmless material by high temperature incineration technique by the application, enter air, make three waste discharge reach the environmental protection standard of country, do not produce secondary pollution, and the heat recovery that will produce in burning process.
Accompanying drawing explanation
Fig. 1 be the application animals with diseases high temperature degradation after the structural representation of waste liquid burned waste gas device；
Fig. 2 be the application animals with diseases high temperature degradation after the process chart of waste liquid burned waste gas device.
Detailed description of the invention
Below, with reference to accompanying drawing, this utility model is more fully illustrated, shown in the drawings of exemplary embodiment of the present utility model.But, this utility model can be presented as multiple multi-form, is not construed as the exemplary embodiment being confined to describe here.And it is to provide these embodiments, so that this utility model is fully and completely, and scope of the present utility model is fully conveyed to those of ordinary skill in the art.
For ease of explanation, here can use such as " on ", the space relative terms such as D score " left " " right ", for shown in explanatory diagram a element or feature relative to another element or the relation of feature.It should be understood that in addition to the orientation shown in figure, spatial terminology is intended to include device different azimuth in use or operation.Such as, if the device in figure is squeezed, be stated as being positioned at the element of other elements or feature D score will be located into other elements or feature " on ".Therefore, exemplary term D score can comprise upper and lower both orientation.Device can otherwise position (90-degree rotation or be positioned at other orientation), relatively illustrates used herein of space correspondingly to explain.
As shown in Figure 1-2, after the animals with diseases high temperature degradation of the application, waste liquid burned waste gas device includes being sequentially connected with closed crushing device, high pressure-temperature bactericidal unit 1, fat separator device, fermentative degradation device, waste liquid burned waste gas device 2, residual heat using device 3, heat exchanger 4, spray-absorption device 5, mist water separator 6；Wherein, described closed crushing device, for being crushed by the corpse of animals with diseases, crushes and is delivered to described high pressure-temperature bactericidal unit 1 afterwards；The corpse of the described high pressure-temperature bactericidal unit 1 animals with diseases after crushing carries out high temperature sterilize, afterwards waste liquid and oils and fats is delivered to described fat separator device, residue is delivered to described fermentative degradation device；Described fat separator device is for separating described waste liquid and oils and fats, and isolated oils and fats uses as biodiesel raw material, and isolated waste liquid enters described waste liquid burned waste gas device；It is organic fertilizer that described fermentative degradation device is used for described residue fermentative degradation；Described waste liquid burned waste gas device 2 is for being converted into high-temperature flue gas by described waste liquid through high-temp combustion, and described high-temperature flue gas is delivered to described residual heat using device 3；Described residual heat using device 3 is for carrying out UTILIZATION OF VESIDUAL HEAT IN to described high-temperature flue gas, and the waste heat recycled is delivered to the steam feeding autoclave sterilization system that the waste heat boiler after described high pressure-temperature bactericidal unit 1(the application will burn produces, maximization utilizes, operating cost is reduced for enterprise's burning disposal, reach the purpose of resource circulation utilization), by lowering the temperature, later flue gas is delivered to described heat exchanger 4；Described heat exchanger 4 is for carrying out waste heat recycling to later flue gas of lowering the temperature, and the waste heat recycled is delivered to described waste liquid burned waste gas device 2, waste heat recycles later flue gas and is delivered to described spray-absorption device 5；Described spray-absorption device 5 is used for absorbing remaining deleterious acidic gas and little granule dust in removal flue gas；Then flue gas being delivered to described mist water separator 6, described mist water separator 6 water in flue gas and gas is separated, the gas after separation is sent into chimney 15 through air-introduced machine 20 and enters atmosphere.
Incinerator also includes that waste liquid stirs storage tank 7, waste liquid transfer pipeline, Waste liquid atomization jetting device 9；Described waste liquid stirring storage tank 7 will be for being stirred through the isolated waste liquid of described fat separator device, and inputting described Waste liquid atomization jetting device 9 through described waste liquid transfer pipeline after filter 8 filters, the waste liquid after filtration sprays into described waste liquid burned waste gas device 2 after described Waste liquid atomization jetting device 9 is atomized.
Incinerator also includes air compressor 10 and compressed air tunnel；Compressed air is delivered to described Waste liquid atomization jetting device 9 through described compressed air tunnel by described air compressor 10；For the waste liquid after described Waste liquid atomization jetting device 9 is atomized being sprayed into described waste liquid burned waste gas device 2.
Incinerator also includes urgent bypass line 11 and absorbent charcoal adsorber 12, when incinerator operation troubles, the waste gas produced in high pressure-temperature bactericidal unit 1 and fermentative degradation device enters air after described urgent bypass line 11 and absorbent charcoal adsorber 12 process.
Incinerator also includes that oxygenating blower fan 13, described oxygenating blower fan 13 are connected with described heat exchanger 4；For for heat exchanger 4 supplemental oxygen.
Waste liquid burned waste gas device 2 is the stove that a cylindrical inwall is lined with refractory material.Fuel passes through Pipeline transport to waste liquid burned waste gas device 2, in-furnace temperature is made slowly to raise by automatic ignition system, through about half an hour, when the furnace temperature display instrument on switch board shows 850 DEG C, opening Waste liquid atomization jetting device 9 and air compressor 10, be vaporific to spray into 2 the internal burnings of waste liquid burned waste gas device by waste liquid, combustion air is oriented in a tangential direction introducing body of heater by a supervisor along incinerator, the air injected produces a flame cylinder, spirals and discharges from body of heater.nullThe waste liquid rotated and high-temperature combustion gas swash play agitation，There is rapidly oxidation reaction，Burn according to three T principle (temperature、Time、Eddy current) design，After waste liquid enters incinerator，Combustion flame rotates along the main combustion barrel of furnace body with the speed of 2～3 meter per seconds，And axially move along body of heater with the speed of 2～3 meter per seconds，Substantially prolongs the waste liquid time of staying in thermal-flame district，Suppress the airtight fire net that air velocity 2～3 meter per second composition interweaves，Flame eddy current is made fully to be burnt (850-1100 DEG C)，High-temperature flue gas enters residual heat using device 3 and carries out UTILIZATION OF VESIDUAL HEAT IN，After flue gas entrance G-G heat exchanger after cooling carries out UTILIZATION OF VESIDUAL HEAT IN，Flue gas after burning is then to adding alkali spray-absorption device，Absorb and remove remaining deleterious acidic gas and little granule dust in flue gas，Gas up to standard after process is sent into chimney through air-introduced machine and enters atmosphere.
Organic exhaust gas is introduced body of heater by waste gas nozzle 18, start-up burner light, and with waste liquid one combust, the gas simultaneous reactions with burning burns at high operating temperatures, (whole combustion process is for automatically controlling).
Residual heat using device 3 is waste heat boiler；Incinerator also includes electric-control system and temperature control system, and described electric-control system is implemented power supply for power-equipment each to waste disposal facilities and automatically controls；Described temperature control system is for being monitored and controlled the temperature in burning process and flame.
Being provided with temperature sensor in waste liquid burned waste gas device, described temperature sensor is connected with described temperature control system, for providing the temperature information in waste liquid burned waste gas device to described temperature control system.
Being provided with burner in waste liquid burned waste gas device, the open and close of described burner are by described electric control system controls；After described burner starts, when making temperature in waste liquid burned waste gas device be promoted to 900-1100 DEG C, burner extinguishes, and when in-furnace temperature drops to 850 DEG C, burner is automatically lighted and again heated, runs so forth.
In Fig. 2,14 is flue, waste liquid burned waste gas device 2 is additionally provided with venting 16 and ash hole 17, and is additionally provided with auxiliary burner 19 and auxiliary fuel in the bottom of waste liquid burned waste gas device 2.
For ensureing the properly functioning of waste treatment system, the design reaches the safety protection function (having a power failure suddenly and waste gas entrance emergency bypass under malfunction at equipment) of temperature control burning and automatic interlock by gathering the parameter variation signal with transmission temperature.
Described above simply to illustrate that this utility model, it is understood that this utility model is not limited to above example, meets the various variants of this utility model thought all within protection domain of the present utility model.
Claims (10)
1. waste liquid burned waste gas device after an animals with diseases high temperature degradation, it is characterized in that, closed crushing device that described incinerator includes being sequentially connected with, high pressure-temperature bactericidal unit, fat separator device, fermentative degradation device, waste liquid burned waste gas device, residual heat using device, heat exchanger, spray-absorption device, mist water separator；Wherein,
Described closed crushing device, for being crushed by the corpse of animals with diseases, crushes and is delivered to described high pressure-temperature bactericidal unit afterwards；
The corpse of described high pressure-temperature bactericidal unit animals with diseases after crushing carries out high temperature sterilize, afterwards waste liquid and oils and fats is delivered to described fat separator device, residue is delivered to described fermentative degradation device；
Described fat separator device is for separating described waste liquid and oils and fats, and isolated oils and fats uses as biodiesel raw material, and isolated waste liquid enters described waste liquid burned waste gas device；
It is organic fertilizer that described fermentative degradation device is used for described residue fermentative degradation；
Described waste liquid burned waste gas device is for being converted into high-temperature flue gas by described waste liquid through high-temp combustion, and described high-temperature flue gas is delivered to described residual heat using device；
Described residual heat using device for carrying out UTILIZATION OF VESIDUAL HEAT IN to described high-temperature flue gas, and the waste heat recycled is delivered to described high pressure-temperature bactericidal unit, and by lowering the temperature, later flue gas is delivered to described heat exchanger；
Described heat exchanger is for carrying out waste heat recycling to later flue gas of lowering the temperature, and the waste heat recycled is delivered to described waste liquid burned waste gas device, waste heat recycles later flue gas and is delivered to described spray-absorption device；
Described spray-absorption device is used for absorbing remaining deleterious acidic gas and little granule dust in removal flue gas；Then flue gas being delivered to described mist water separator, described mist water separator the water in flue gas and gas is separated, the gas after separation is sent into chimney through air-introduced machine and enters atmosphere.
Waste liquid burned waste gas device after animals with diseases high temperature degradation the most according to claim 1, it is characterised in that described incinerator also includes that waste liquid stirs storage tank, waste liquid transfer pipeline, Waste liquid atomization jetting device；Described waste liquid stirring storage tank will be for being stirred through the isolated waste liquid of described fat separator device, and inputting described Waste liquid atomization jetting device through described waste liquid transfer pipeline after filtering, the waste liquid after filtration sprays into described waste liquid burned waste gas device after described Waste liquid atomization jetting device is atomized.
Waste liquid burned waste gas device after animals with diseases high temperature degradation the most according to claim 2, it is characterised in that described incinerator also includes air compressor and compressed air tunnel；Compressed air is delivered to described Waste liquid atomization jetting device through described compressed air tunnel by described air compressor；For the waste liquid after described Waste liquid atomization jetting device is atomized is sprayed into described waste liquid burned waste gas device.
Waste liquid burned waste gas device after animals with diseases high temperature degradation the most according to claim 1, it is characterized in that, described incinerator also includes urgent bypass line and absorbent charcoal adsorber, and the waste gas produced in described high pressure-temperature bactericidal unit and fermentative degradation device enters air after described urgent bypass line and absorbent charcoal adsorber.
Waste liquid burned waste gas device after animals with diseases high temperature degradation the most according to claim 1, it is characterised in that described incinerator also includes that oxygenating blower fan, described oxygenating blower fan are connected with described heat exchanger.
Waste liquid burned waste gas device after animals with diseases high temperature degradation the most according to claim 1, it is characterised in that the inwall that described waste liquid burned waste gas device is cylindrical is lined with the stove of refractory material.
Waste liquid burned waste gas device after animals with diseases high temperature degradation the most according to claim 1, it is characterised in that described residual heat using device is waste heat boiler.
Waste liquid burned waste gas device after animals with diseases high temperature degradation the most according to claim 1, it is characterized in that, described incinerator also includes electric-control system and temperature control system, and described electric-control system is implemented power supply for power-equipment each to waste disposal facilities and automatically controls；Described temperature control system is for being monitored and controlled the temperature in burning process and flame.
Waste liquid burned waste gas device after animals with diseases high temperature degradation the most according to claim 8, it is characterized in that, it is provided with temperature sensor in described waste liquid burned waste gas device, described temperature sensor is connected with described temperature control system, for providing the temperature information in waste liquid burned waste gas device to described temperature control system.
Waste liquid burned waste gas device after animals with diseases high temperature degradation the most according to claim 8, it is characterised in that being provided with burner in described waste liquid burned waste gas device, the open and close of described burner are by described electric control system controls；After described burner starts, when making temperature in waste liquid burned waste gas device be promoted to 900-1100 DEG C, burner extinguishes, and when in-furnace temperature drops to 850 DEG C, burner is automatically lighted and again heated, runs so forth.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201620446090.1U CN205640917U (en) | 2016-05-17 | 2016-05-17 | Disease animals high temperature degradation back waste liquid waste gas burns device |
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| CN201620446090.1U CN205640917U (en) | 2016-05-17 | 2016-05-17 | Disease animals high temperature degradation back waste liquid waste gas burns device |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105823048A (en) * | 2016-05-17 | 2016-08-03 | 宜兴市智博环境设备有限公司 | Incineration device for waste liquid and waste gas which are generated during diseased animal high-temperature degradation |
| CN106278436A (en) * | 2016-10-15 | 2017-01-04 | 南宁绿智环保科技有限公司 | A kind of method and device of solid organic matters aerobic pressurized high-temperature fermentation |
| CN106747694A (en) * | 2016-12-16 | 2017-05-31 | 凌桂掌 | The environmental protection of birds corpse recycles processing unit |
| CN112206655A (en) * | 2020-09-28 | 2021-01-12 | 浙江遗爱环保科技服务有限公司 | Flue gas purification device of pet incineration car |
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2016
- 2016-05-17 CN CN201620446090.1U patent/CN205640917U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105823048A (en) * | 2016-05-17 | 2016-08-03 | 宜兴市智博环境设备有限公司 | Incineration device for waste liquid and waste gas which are generated during diseased animal high-temperature degradation |
| CN105823048B (en) * | 2016-05-17 | 2018-03-27 | 宜兴市智博环境设备有限公司 | Waste liquid burned waste gas device after a kind of animals with diseases high temperature degradation |
| CN106278436A (en) * | 2016-10-15 | 2017-01-04 | 南宁绿智环保科技有限公司 | A kind of method and device of solid organic matters aerobic pressurized high-temperature fermentation |
| CN106747694A (en) * | 2016-12-16 | 2017-05-31 | 凌桂掌 | The environmental protection of birds corpse recycles processing unit |
| CN106747694B (en) * | 2016-12-16 | 2022-08-19 | 凌桂掌 | Poultry corpse environmental protection recycle processing apparatus |
| CN112206655A (en) * | 2020-09-28 | 2021-01-12 | 浙江遗爱环保科技服务有限公司 | Flue gas purification device of pet incineration car |
| CN112206655B (en) * | 2020-09-28 | 2022-03-04 | 浙江遗爱环保科技服务有限公司 | Flue gas purification device of pet incineration car |
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Granted publication date: 20161012 Termination date: 20180517 |