CN105032042B - Full-automatic waste gas, waste water and waste residue treatment system - Google Patents
Full-automatic waste gas, waste water and waste residue treatment system Download PDFInfo
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- CN105032042B CN105032042B CN201510466532.9A CN201510466532A CN105032042B CN 105032042 B CN105032042 B CN 105032042B CN 201510466532 A CN201510466532 A CN 201510466532A CN 105032042 B CN105032042 B CN 105032042B
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Abstract
A full-automatic waste gas, waste water and waste residue treatment system comprises a purifying tower. The treatment system further comprises rubber powder separators including the first rubber powder separator and the second rubber powder separator. An air inlet is formed in the side wall of the upper end of the first rubber powder separator. The lower end of the first rubber powder separator is connected with the upper end of the second rubber powder separator. The upper surface of the first rubber powder separator is connected with one end of a first guide pipe. The other end of the first guide pipe is connected with one end of a concentric-circle-shaped pipe. The other end of the concentric-circle-shaped pipe is connected with one end of a second guide pipe. The other end of the second guide pipe is connected with a first separator. The first separator is installed on the upper portion of a flotation chamber installed in the purifying tower. The second guide pipe is further connected with a chemical metering pump which is connected with a chemical box. The treatment system can achieve step-by-step separation of waste gas, waste water and waste residues and eliminates the situation that existing equipment is not thorough in treatment, and treated tail gas accords with national standards. Besides, excessive manual operation is not needed in the whole process, and the workload of workers is reduced.
Description
Technical field
The present invention relates to full-automatic waste gas, waste water, Solid state fermentation system, belong to rubber tail gas processing equipment technology neck
Domain.
Background technology
In China, due to the industrial waste gas that rubber tyre industry produces have malodorous quality, large-minded, complicated component,
The features such as grain thing content is high, does not have a kind of professional equipment being specifically designed for such industrial waste gas process, and the technology of process is relatively stagnant
Afterwards, the exhaust gas treatment technology of current the sector mainly has following several, all there is certain defective.Masking method in principle simultaneously
Really waste gas is not removed, but the mode of deception olfactory sensation, conventional vegetation water or biological fluid can increase volatility in waste gas and have
Machine chemical compound gas content；Absorption method is easily saturated inefficacy, produces secondary pollution it is impossible to be used for the industry deodorization simultaneously；Spray
Method and bioanalysises can not be processed for water-fast Organic substance in such waste gas, and gas-liquid mass transfer is slowly it is impossible to reach process simultaneously
Effect；Because such waste gas is large-minded, fuel value is too low simultaneously, therefore combustion method inapplicable the industry deodorization；Ultraviolet photolysis skill
Art oxidation efficiency is low, and in this industry application, equipment needed thereby volume is too big, fluorescent tube quantity is too many, simultaneously because ultraviolet lamp tube uses
Short life, leads to once to put into all very high with operating cost；Plasma method needs waste gas and discharge medium directly contact, leads to put
Electrolyte is easily corroded or poison deactivation, is not suitable for the industry exhaust-gas treatment.
So be badly in need of now a can effective process rubber industry wastewater recycle during produce the equipment of waste gas.
Content of the invention
The present invention devises full-automatic waste gas, waste water, Solid state fermentation system to solve the above problems, and its object is to:
Waste gas, waste water and waste residue can be efficiently separated out by the present invention, produce during fully solving rubber industry wastewater recycling is useless
Thing.
The purpose of the present invention is achieved through the following channels:
Full-automatic waste gas, waste water, Solid state fermentation system, including purifying column it is characterised in that described processing system also includes
Rubber powder separator, vapour liquid separator, described rubber powder separator includes the first rubber powder separator and the second rubber powder separator, and described
It is provided with air inlet, the first rubber powder separator lower end and the second rubber powder separator upper end are even on one rubber powder separator upper end side wall
Connect, described first rubber powder separator upper surface and the first tube at one end connect, the first conduit other end and back-shaped pipe one end connect,
The described back-shaped pipe other end and the second tube at one end connect, and the described second conduit other end and the first separator connect, and described the
One separator is arranged on above gas-floating chamber, and described gas-floating chamber is arranged on inside purifying column, described second conduit also with medication dosing
Pump connects, and described medication dosing pump is also connected with medicine-chest；Described back-shaped pipe is arranged on inside heat exchanger, described heat exchange
Device lower end is provided with water inlet, and heat exchanger upper end is provided with outlet, and described heat exchanger is arranged on above purifying column,
Connect with the 3rd tube at one end on the left of described purifying column lower end, the 3rd conduit other end and squeezer connect, and described squeezer is also
It is connected with the 4th tube at one end, the 4th conduit other end and liquid reservoir pond connect, described liquid reservoir pond and water feeding of water pump end
Connect, water pump water outlet end and the 5th tube at one end connect, the 5th conduit other end and the 6th conduit connect, described 6th conduit one
Connect on the right side of end and purifying column upper end, the 6th conduit other end and water filter connect；Described liquid reservoir pond is also by the 7th
Conduit is connected with the first vapour liquid separator and the second vapour liquid separator, with the 8th conduit on the left of described first vapour liquid separator lower end
One end connects, connection, described first vapour liquid separator upper end and the 9th conduit on the right side of the 8th conduit other end and purifying column upper end
One end connect, on the left of the 9th conduit other end and the second vapour liquid separator lower end connect, described second vapour liquid separator also with combustion
Burn room to connect.
As the optimization further of this programme, described first rubber powder separator lower end and the second rubber powder separator lower end are all pacified
Equipped with wind sheltering device.
As the optimization further of this programme, described second conduit and the 3rd conduit are mounted on control valve, described
On five conduits, check-valves are installed, between described 6th conduit and water filter, check-valves are also installed.
As the optimization further of this programme, on the left of described purifying column, upper end and the tenth tube at one end connect, the tenth conduit
The other end and oily self-cleaning filter connect.
As the optimization further of this programme, described oil self-cleaning filter include left oil self-cleaning filter and right oil from
Cleaning filter, described left oil self-cleaning filter sidewall upper and the 12nd tube at one end connect, the 12nd conduit other end
Connect with the 13rd conduit, described 13rd tube at one end and right oil self-cleaning filter sidewall upper connect, the 13rd conduit
The other end and squeezer connect；On the right side of described left oil self-cleaning filter, lower end and the 14th tube at one end connect, and the 14th leads
The pipe other end and the 15th conduit connect, the 15th tube at one end and connecting with right oil self-cleaning filter side wall lower ends, the tenth
The five conduit other ends and the 5th conduit connect；On described 12nd conduit, the 13rd conduit, the 14th conduit and the 15th conduit
It is mounted on control valve.
As the optimization further of this programme, molten vapour release is installed above described first separator, described molten vapour is released
Put device and molten soda pop delivery pipe one end connects, the molten soda pop delivery pipe other end and molten steam chest lower end connect, described molten steam chest upper end
It is provided with polyhedron empty ball filler.
As the optimization further of this programme, described molten steam chest upper end is provided with blowpipe, air gauge and
11 conduits.
As the optimization further of this programme, described blowpipe one end and molten steam chest, blowpipe
The other end and air pump connect；Described 11st conduit and molten steam chest, the 11st conduit other end and molten vapour cycle pump connect, shown
Molten vapour cycle pump connects also by the 16th conduit and purifying column.
As the optimization further of this programme, in described purifying column, it is additionally provided with liquidometer and gas securing device.
As the optimization further of this programme, described gas securing device includes at least four pieces deflectors, described deflector
By rotation shaft regulated angle.
The invention has the advantages that:
The present invention can realize progressively separating of waste gas, waste water and waste residue, solve existing equipment and process halfway feelings
Condition, makes the tail gas after process meet national standard, and whole process need not the artificial amount of labour crossed multioperation, reduce workman；
The You Heshui that the present invention produces also separately is processed, and is not in obstruction conduit situation, and is easy to the cleaning of whole device；
Slag, water, gas are focused on by the present invention, and small volume has saved land resource；Self-cleaning equipment using water wisely, has reached low
The requirement that carbocyclic ring is protected.
Brief description
Below in conjunction with the accompanying drawings the present invention is described in further detail:
Fig. 1 is present configuration schematic diagram；
Fig. 2 is mplifying structure schematic diagram at Fig. 1 a；
In figure, the 1, first rubber powder separator, the 2, second rubber powder separator, 3, wind sheltering device, 4, air inlet, the 5, first conduit,
6th, back-shaped pipe, the 7, second conduit, the 8, first separator, 9, gas-floating chamber, 10, medication dosing pump, 11, medicine-chest, the 12, the 4th conduit,
13rd, the 5th conduit, 14, water pump, 15, liquid reservoir pond, the 16, the 7th conduit, the 17, first vapour liquid separator, the 18, the 8th conduit,
19th, the 9th conduit, the 20, second vapour liquid separator, 21, combustor, 22, squeezer, the 23, the 3rd conduit, the 24, the 13rd conduit,
25th, the tenth conduit, 26, molten vapour release, 27, molten soda pop delivery pipe, 28, molten steam chest, 29, polyhedron empty ball filler, 30, compression
Air delivery pipe, 31, air gauge, the 32, the 11st conduit, 33, air pump, 34, molten vapour cycle pump, the 35, the 16th conduit, 36, enter
The mouth of a river, 37, outlet, 38, heat exchanger, 39, deflector, 40, liquidometer, 41, rotating shaft, 42, check-valves, 43, control valve,
44th, the 6th conduit, 45, water filter, the 46, the 14th conduit, 47, left oil self-cleaning filter, 48, right oil self-cleaning filtering
Device, the 49, the 12nd conduit, the 50, the 15th conduit, 51, purifying column.
Specific embodiment
All accompanying drawings are only easy to explain basic condition of the present invention below, by the group constituting preferred embodiment in accompanying drawing
The extension of number of packages mesh, position, relation and size will have been described, related change after reading and understanding the situation of the present invention
Implement to belong to industry technical ability.In addition, after the situation of reading and the understanding present invention, coordinating specific strength, weight, intensity and class
The accurate dimension seemingly requiring and the change of dimension scale also fall within industry technical ability.
In different figures same or like assembly is indicated with identical label；In addition it is understood that such as " first " in literary composition,
" second ", " the 3rd ", " on ", D score, "front", "rear", " interior ", " outward ", " end ", " portion ", " section ", " width ", " thickness ", " area "
Etc. and similar term be only easy to observer with reference in figure construction and be only used for help describe the present invention.
Embodiment:
As depicted in figs. 1 and 2, full-automatic waste gas, waste water, Solid state fermentation system, including purifying column, described processing system is also
Including rubber powder separator, vapour liquid separator, described rubber powder separator include the first rubber powder separator 1(for separate rubber powder solid
And gas, gas is carried out to the rubber powder in gas separating by eddy flow.) and the second rubber powder separator 2(is for separation rubber powder admittedly
Body and gas, discharge to the rubber powder after separation.), described first rubber powder separator upper end side wall is provided with air inlet 4, first
Rubber powder separator lower end and the connection of the second rubber powder separator upper end, described first rubber powder separator upper surface and the first conduit 5 one
End connects, and the first conduit other end and back-shaped pipe 6 one end connect, and the described back-shaped pipe other end and the second conduit 7 one end connect, institute
State the second conduit other end and the first separator 8 connects, described first separator is arranged on above gas-floating chamber 9, described gas-floating chamber
Be arranged on inside purifying column 51, described second conduit is also connected with medication dosing pump 10, described medication dosing pump also with medicine-chest 11
Connect；Described back-shaped pipe is arranged on inside heat exchanger 38, and described heat exchanger lower end is provided with water inlet 36, and heat is handed over
Parallel operation upper end is provided with outlet 37, and described heat exchanger is arranged on above purifying column, on the left of described purifying column lower end and the
Three conduit 23 one end connects, and the 3rd conduit other end and squeezer 22 connect, and described squeezer is also with the 4th conduit 12 one end even
Connect, the 4th conduit other end and liquid reservoir pond 15 connect and (for storing the liquid that sludge squeezer is separated, recycle
Reach the demand of low-carbon environment-friendly.), described liquid reservoir pond and water pump 14 water inlet end connect, water pump water outlet end and the 5th conduit 13
One end connects, and the 5th conduit other end and the 6th conduit 44 connect, and connects on the right side of described 6th tube at one end and purifying column upper end,
The 6th conduit other end and water filter 45 connect；Described liquid reservoir pond is also by the 7th conduit 16 and the first vapour liquid separator
17 and second vapour liquid separator 20 connect, on the left of described first vapour liquid separator lower end and the 8th conduit 18 one end connect, the 8th
Connect on the right side of the conduit other end and purifying column upper end, described first vapour liquid separator upper end and the 9th conduit 19 one end connect, the
Connect on the left of the nine conduit other ends and the second vapour liquid separator lower end, described second vapour liquid separator is also connected with combustor 21
(remaining part harmful gass are carried out burning and generates carbon dioxide and vapor qualified discharge.).
As the optimization further of this programme, described first rubber powder separator lower end and the second rubber powder separator lower end are all pacified
Equipped with wind sheltering device 3.
As the optimization further of this programme, described second conduit and the 3rd conduit are mounted on control valve 43, described
On 5th conduit, check-valves are installed, between described 6th conduit and water filter, check-valves 42 are also installed.
As the optimization further of this programme, on the left of described purifying column, upper end and the tenth conduit 25 one end connect, and the tenth leads
The pipe other end and oily self-cleaning filter connect.
As the optimization further of this programme, described oil self-cleaning filter includes left oil self-cleaning filter 47 and right oil
Self-cleaning filter 48, described left oil self-cleaning filter sidewall upper and the 12nd conduit 49 one end connect, the 12nd conduit
The other end and the 13rd conduit 24 connect, and described 13rd tube at one end and right oil self-cleaning filter sidewall upper connect, the
The 13 conduit other ends and squeezer connect；On the right side of described left oil self-cleaning filter, lower end and the 14th conduit 46 one end connect
Connect, the 14th conduit other end and the 15th conduit 50 connect, the 15th tube at one end and and right oil self-cleaning filter side wall
Lower end connects, and the 15th conduit other end and the 5th conduit connect；Described 12nd conduit, the 13rd conduit, the 14th conduit
It is mounted on control valve with the 15th conduit.
As the optimization further of this programme, molten vapour release 26, described molten vapour are installed above described first separator
Release and molten soda pop delivery pipe 27 one end connect, and the molten soda pop delivery pipe other end and molten steam chest 28 lower end connect, described molten vapour
Room upper end is provided with polyhedron empty ball filler 29(polyhedron empty ball filler, increases the dissolved oxygen of molten steam chest, improves oil-water separation effect
Really.).
As the optimization further of this programme, described molten steam chest upper end is provided with blowpipe 30, air gauge 31
With the 11st conduit 32.
As the optimization further of this programme, described blowpipe one end and molten steam chest, blowpipe
The other end and air pump 33 connect；Described 11st conduit and molten steam chest, the 11st conduit other end and molten vapour cycle pump 34 connect,
Shown molten vapour cycle pump connects also by the 16th conduit 35 and purifying column.
As the optimization further of this programme, in described purifying column, it is additionally provided with liquidometer 40 and gas securing device (gas
Body securing device adjusts gas flow rate so that gas is stable, plays oil, water, slag centrifugation.).
As the optimization further of this programme, described gas securing device includes at least four pieces deflectors 39, described water conservancy diversion
Plate adjusts angle by rotating shaft 41.
Concrete operating principle:
As depicted in figs. 1 and 2, vapour is discharged to retort, we take recovery heat, deep condensation, coolant to circulate
Method is processed to retort discharge gas.The cardinal principle of this technique is: by heat recovery and deep condensation so that water steams
Vapour and before entering tank be liquid or solid-state predominantly organic pollutant (Carbon bisulfide, carbon tetrachloride, ethane, nitrogen, leucoaurin, sulfuration
Hydrogen, methanthiol, methane thial, methyl disulfide) condense out, and add chemical agent (Alumen and ferrous sulfate) to organic pollution
Carry out reacting, process.After standing separation, water add retort recycle, oil and impurity periodic cleaning go out after as softening agent
Use.A small amount of high boiling point organic compound and sulfide are removed with direct burning, catalytic combustion method.Realize waste steam exhausting up to standard, useless
Water zero discharge.
The high-temperature steam that digester is discharged, initially enters rubber powder separator after valve decompression, isolates in gas and carry secretly
The debris such as rubber powder, avoid blocking pipeline.High temperature gas after removing foreign matter, enters heat recoverer, enters back into depth cold
Condenser, in this equipment, the cooling water relatively low with temperature carries out heat exchange, and steam is got off by total condensation, discharges with high temperature gas
Most of Organic substance is also condensed simultaneously.Condensed fluid enter collect carry out in separator settlement separate.A small amount of incondensable gas warp
Jet absorber is drawn, washs, enter terminal processing device directly burns, catalytic combustion method removes, and removes hydrogen sulfide, organic
The gas that thing etc. is poisonous, is harmful to, has people's taste of choking, discharges after meeting environment protection emission requirement.
Enter from deep condenser condensed fluid out collect in separator, oil, water, solid impurity settlement separate.Oil wafts
Float on top, periodically discharge from top oil drain out；Heavy solid impurity is deposited on device bottom, periodically from bottom inspection socket
Clear；Isolate the clean water after the impurity such as greasy dirt (Organic substance) and digester reuse is sent back to by condensate pump.
Using water seal safety device it is ensured that system is run under the pressure less than 0.08mpa, no pressure tankage.
Jet absorber adopts water-jet to aspirate, and the system that enables to is run under negative pressure state, thus ensureing desulfurization
Thorough, the remaining gas of tank steam discharge is few.Waterpower aspiration procedure is also to gas washing, absorption process, can effectively remaining vapour be carried out
Deep purifying.Total system supplements water first as the supplementary water of Jet absorber water so that having in Jet absorber water
Machine thing remains relatively low concentration, improves the washing to remaining vapour, assimilation effect.
Specific work process:
As depicted in figs. 1 and 2, the air in production process is discharged in tank, through the first rubber powder separator and the second rubber powder
Separator rotation, solid and gas is separated, and after gas is discharged, solid sinks.Expellant gas are cooled down by heat exchanger, and (hot water can
For domestic water).Chemical agent enters purifying column by medication dosing pump, and the laggard circulation of qi promoting that waste water carried out flocculate is floated, can be real
Existing oil-water separation.The purifying column reservoir portion of the present invention reduces, and improves core intersection.Envisaged underneath gas firmware, to gas
Floatation surface is suitably consolidated, and reaches oil-water separation and maximizes.The a set of air-floating apparatus of tank body envisaged underneath, using air itself pressure
Power, carries out air supporting to sewage, reduces the impact that gas consolidates to mud as far as possible.Oil drawer makes oil from outflow by the height of itself
Come.By oil strainer, the dregs of fat are separated, the dregs of fat pass through self-stripping unit and waste residue discharged feeding filtration squeezer, after sedimentation
Mud is separated by filtering squeezer and carrying out pulp water, and after coagulation, clear water is discharged by filter, the waste residue that the coagulation of pettiness gets off
After automatic cleaning, it is discharged to filtration squeezer and is processed.Gas by washing with water after, chemically treated device is by moieties
Processed, the gas after process enters and carries out aerosol separation subsequently into combustion chambers burn every day with fog, and the gas after burning can
Qualified discharge.Increase a set of airfloat equipment, this equipment no air is entered fashionable also can accomplish air supporting act on, oil is carried out to sewage
All sewage can be played certain treatment effect by the detached function of water.
Self-cleaning work process is:
As shown in Fig. 2 when needing to filter the dregs of fat, the control valve of the tenth catheter guide tube is opened, left oil self-cleaning filter
Also open with the control valve of right oil self-cleaning filter lower end, close the 12nd conduit, the 13rd conduit, the 14th conduit and the
15 supravasal control valves；When needing self-cleaning, the control valve of the tenth catheter guide tube is closed, left oil self-cleaning filtering
Device and right oil self-cleaning filter lower end control valve be also switched off, open the 12nd conduit, the 13rd conduit, the 14th conduit and
15th supravasal control valve, opens water pump, and impurity filters through squeezer again.
The basic teaching of the present invention is illustrated, and for having the people of the usual technical ability in this area, many extends and becomes
Change will be aobvious and the person of being apparent from.Because the present invention that description discloses can be in the other spies without departing from present invention spirit or general characteristics
Setting formula is implementing, and some forms of these particular forms have been noted, so, description embodiments of the disclosure should be regarded as
Illustrate rather than restriction.The scope of the present invention is to be defined by appended claim, rather than by described above institute circle
Calmly, within the scope of all changes of the impartial meaning and scope that fall into claim still being will be contained in it.
The present invention produces a desired effect.
Claims (10)
1. full-automatic waste gas, waste water, Solid state fermentation system, including purifying column it is characterised in that described processing system also includes glue
Powder separator, vapour liquid separator, described rubber powder separator includes the first rubber powder separator and the second rubber powder separator, and described first
It is provided with air inlet, the first rubber powder separator lower end and the second rubber powder separator upper end connect on rubber powder separator upper end side wall,
Described first rubber powder separator upper surface and the first tube at one end connect, and the first conduit other end and back-shaped pipe one end connect, institute
State the back-shaped pipe other end and the second tube at one end connects, the described second conduit other end and the first separator connect, described first
Separator is arranged on above gas-floating chamber, and described gas-floating chamber is arranged on inside purifying column, described second conduit also with medication dosing pump
Connect, described medication dosing pump is also connected with medicine-chest；Described back-shaped pipe is arranged on inside heat exchanger, described heat exchanger
Lower end is provided with water inlet, and heat exchanger upper end is provided with outlet, and described heat exchanger is arranged on above purifying column, institute
State on the left of purifying column lower end and the 3rd tube at one end connect, the 3rd conduit other end and squeezer connect, described squeezer also with
4th tube at one end connects, and the 4th conduit other end and liquid reservoir pond connect, and described liquid reservoir pond and water feeding of water pump end are even
Connect, water pump water outlet end and the 5th tube at one end connect, the 5th conduit other end and the 6th conduit connect, described 6th tube at one end
Connect with the right side of purifying column upper end, the 6th conduit other end and water filter connect；Described liquid reservoir pond is led also by the 7th
Pipe is connected with the first vapour liquid separator and the second vapour liquid separator, with the 8th conduit one on the left of described first vapour liquid separator lower end
End connects, connection, described first vapour liquid separator upper end and the 9th conduit one on the right side of the 8th conduit other end and purifying column upper end
End connect, on the left of the 9th conduit other end and the second vapour liquid separator lower end connect, described second vapour liquid separator also with burning
Room connects.
2. full-automatic waste gas according to claim 1, waste water, Solid state fermentation system it is characterised in that: described first rubber powder
Separator lower end and the second rubber powder separator lower end are mounted on wind sheltering device.
3. full-automatic waste gas according to claim 1, waste water, Solid state fermentation system it is characterised in that: described second conduit
It is mounted on control valve with the 3rd conduit, described 5th conduit is provided with check-valves, described 6th conduit and water filter
Between check-valves are also installed.
4. full-automatic waste gas according to claim 1, waste water, Solid state fermentation system it is characterised in that: described purifying column is left
Side upper end and the tenth tube at one end connect, and the tenth conduit other end and oily self-cleaning filter connect.
5. full-automatic waste gas according to claim 4, waste water, Solid state fermentation system it is characterised in that: described oil self-cleaning
Filter includes left oil self-cleaning filter and right oil self-cleaning filter, described left oil self-cleaning filter sidewall upper and the
12 tube at one end connect, and the 12nd conduit other end and the 13rd conduit connect, and described 13rd tube at one end and right oil are certainly
Cleaning filter wall upper end connects, and the 13rd conduit other end and squeezer connect；On the right side of described left oil self-cleaning filter
Lower end and the 14th tube at one end connect, and the 14th conduit other end and the 15th conduit connect, the 15th tube at one end and and
Right oil self-cleaning filter side wall lower ends connect, and the 15th conduit other end and the 5th conduit connect；Described 12nd conduit,
It is mounted on control valve on 13 conduits, the 14th conduit and the 15th conduit.
6. full-automatic waste gas according to claim 1, waste water, Solid state fermentation system it is characterised in that: described first separate
Molten vapour release is installed above device, described molten vapour release and molten soda pop delivery pipe one end connect, and molten soda pop delivery pipe is another
End and molten steam chest lower end connect, and described molten steam chest upper end is provided with polyhedron empty ball filler.
7. full-automatic waste gas according to claim 6, waste water, Solid state fermentation system it is characterised in that: on described molten steam chest
End is provided with blowpipe, air gauge and the 11st conduit.
8. full-automatic waste gas according to claim 7, waste water, Solid state fermentation system it is characterised in that: described compressed air
Delivery pipe one end and molten steam chest, the blowpipe other end and air pump connect；Described 11st conduit and molten steam chest, the tenth
The one conduit other end and molten vapour cycle pump connect, and shown molten vapour cycle pump connects also by the 16th conduit and purifying column.
9. full-automatic waste gas according to claim 7, waste water, Solid state fermentation system it is characterised in that: in described purifying column
It is additionally provided with liquidometer and gas securing device.
10. full-automatic waste gas according to claim 9, waste water, Solid state fermentation system it is characterised in that: described gas is steady
It is fixedly mounted with and puts including at least four pieces of deflectors, described deflector is by rotation shaft regulated angle.
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| CN201510466532.9A CN105032042B (en) | 2015-08-03 | 2015-08-03 | Full-automatic waste gas, waste water and waste residue treatment system |
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| CN108784426B (en) * | 2017-04-26 | 2021-06-18 | 佛山市顺德区美的电热电器制造有限公司 | Soybean milk maker and control method and control device thereof |
| CN107998821A (en) * | 2017-12-30 | 2018-05-08 | 和和乐和（天津）环境科技有限公司 | A kind of fixed bed zeolite VOC exhaust treatment systems |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001207172A (en) * | 2000-01-31 | 2001-07-31 | Morooka:Kk | Movable carbonizing furnace |
| US6534689B1 (en) * | 2001-08-24 | 2003-03-18 | Pyrocat Ltd. | Process for the conversion of waste plastics to produce hydrocarbon oils |
| CN1746263A (en) * | 2005-09-22 | 2006-03-15 | 华南再生资源（中山）有限公司 | Waste plastic and rubber reduction and reducing system |
| CN2866503Y (en) * | 2005-09-22 | 2007-02-07 | 华南再生资源（中山）有限公司 | Recovery system for treating waste plastic and rubber |
| KR101200479B1 (en) * | 2011-01-19 | 2012-11-12 | 에이치투더블유티이 주식회사 | Treating system of waste materials |
| CN203447935U (en) * | 2013-08-27 | 2014-02-26 | 昆山工统环保机械有限公司 | Organic waste gas adsorption-desorption concentration catalytic burning device system |
| CN204911025U (en) * | 2015-08-03 | 2015-12-30 | 沭阳嘉盛再生资源有限公司 | Full -automatic waste gas, waste water, waste residue processing system |
-
2015
- 2015-08-03 CN CN201510466532.9A patent/CN105032042B/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001207172A (en) * | 2000-01-31 | 2001-07-31 | Morooka:Kk | Movable carbonizing furnace |
| US6534689B1 (en) * | 2001-08-24 | 2003-03-18 | Pyrocat Ltd. | Process for the conversion of waste plastics to produce hydrocarbon oils |
| CN1746263A (en) * | 2005-09-22 | 2006-03-15 | 华南再生资源（中山）有限公司 | Waste plastic and rubber reduction and reducing system |
| CN2866503Y (en) * | 2005-09-22 | 2007-02-07 | 华南再生资源（中山）有限公司 | Recovery system for treating waste plastic and rubber |
| KR101200479B1 (en) * | 2011-01-19 | 2012-11-12 | 에이치투더블유티이 주식회사 | Treating system of waste materials |
| CN203447935U (en) * | 2013-08-27 | 2014-02-26 | 昆山工统环保机械有限公司 | Organic waste gas adsorption-desorption concentration catalytic burning device system |
| CN204911025U (en) * | 2015-08-03 | 2015-12-30 | 沭阳嘉盛再生资源有限公司 | Full -automatic waste gas, waste water, waste residue processing system |
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| CN105032042A (en) | 2015-11-11 |
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