CN107084596A - The efficient energy-saving drying system and technique of a kind of High water cut material - Google Patents
The efficient energy-saving drying system and technique of a kind of High water cut material Download PDFInfo
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- CN107084596A CN107084596A CN201710445868.6A CN201710445868A CN107084596A CN 107084596 A CN107084596 A CN 107084596A CN 201710445868 A CN201710445868 A CN 201710445868A CN 107084596 A CN107084596 A CN 107084596A
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- 238000001035 drying Methods 0.000 title claims abstract description 534
- 239000000463 material Substances 0.000 title claims abstract description 181
- 238000000034 method Methods 0.000 title claims abstract description 51
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 47
- 230000000694 effects Effects 0.000 claims abstract description 376
- 238000004064 recycling Methods 0.000 claims abstract description 33
- 238000007789 sealing Methods 0.000 claims abstract description 31
- 238000007599 discharging Methods 0.000 claims abstract description 17
- 238000011049 filling Methods 0.000 claims abstract description 3
- 238000007600 charging Methods 0.000 claims description 74
- 208000028659 discharge Diseases 0.000 claims description 73
- 230000000087 stabilizing effect Effects 0.000 claims description 25
- 235000011837 pasties Nutrition 0.000 claims description 22
- 239000000843 powder Substances 0.000 claims description 22
- 239000012065 filter cake Substances 0.000 claims description 21
- 239000011344 liquid material Substances 0.000 claims description 21
- 239000007788 liquid Substances 0.000 claims description 19
- 239000006071 cream Substances 0.000 claims description 18
- 206010013786 Dry skin Diseases 0.000 claims description 17
- 239000000428 dust Substances 0.000 claims description 10
- 238000009826 distribution Methods 0.000 claims description 9
- 239000004744 fabric Substances 0.000 claims description 9
- 239000000203 mixture Substances 0.000 claims description 8
- 230000002209 hydrophobic effect Effects 0.000 claims description 7
- 238000009833 condensation Methods 0.000 claims description 6
- 230000005494 condensation Effects 0.000 claims description 6
- 238000002955 isolation Methods 0.000 claims description 6
- 238000000926 separation method Methods 0.000 claims description 6
- 239000013589 supplement Substances 0.000 claims description 6
- 230000001105 regulatory effect Effects 0.000 claims description 5
- 238000003860 storage Methods 0.000 claims description 5
- 239000012080 ambient air Substances 0.000 claims description 4
- 239000011505 plaster Substances 0.000 claims description 4
- 230000006641 stabilisation Effects 0.000 claims description 4
- 238000011105 stabilization Methods 0.000 claims description 4
- 238000001816 cooling Methods 0.000 claims description 3
- 238000010410 dusting Methods 0.000 claims description 3
- 238000000605 extraction Methods 0.000 claims description 3
- 238000000746 purification Methods 0.000 claims description 3
- 238000011084 recovery Methods 0.000 claims description 3
- 239000010865 sewage Substances 0.000 claims description 3
- 238000001727 in vivo Methods 0.000 claims description 2
- 229920006395 saturated elastomer Polymers 0.000 claims description 2
- 238000001291 vacuum drying Methods 0.000 claims description 2
- 239000007789 gas Substances 0.000 description 35
- 238000005265 energy consumption Methods 0.000 description 9
- 238000010438 heat treatment Methods 0.000 description 6
- 230000007613 environmental effect Effects 0.000 description 4
- 238000004134 energy conservation Methods 0.000 description 3
- 239000012266 salt solution Substances 0.000 description 3
- 239000010802 sludge Substances 0.000 description 3
- 238000010612 desalination reaction Methods 0.000 description 2
- 239000011343 solid material Substances 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000005431 greenhouse gas Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 210000003205 muscle Anatomy 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B7/00—Drying solid materials or objects by processes using a combination of processes not covered by a single one of groups F26B3/00 and F26B5/00
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B20/00—Combinations of machines or apparatus covered by two or more of groups F26B9/00 - F26B19/00
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B23/00—Heating arrangements
- F26B23/10—Heating arrangements using tubes or passages containing heated fluids, e.g. acting as radiative elements; Closed-loop systems
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/001—Handling, e.g. loading or unloading arrangements
- F26B25/002—Handling, e.g. loading or unloading arrangements for bulk goods
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/005—Treatment of dryer exhaust gases
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The present invention relates to water-containing materials technical field of drying, the efficient energy-saving drying system and technique of a kind of High water cut material are disclosed, the efficient energy-saving drying system that the technique is used is connected by the main shaft cavity of an effect drying machine with a heat source system, one effect dryer cavity inner exhaust gas recycles heat source system with indirect steam and connected, and the filling end of an effect dryer cavity is connected by indirect steam replenishment system with a heat source system;The main shaft cavity output end of one effect drying machine is recycled the output end of heat source system, the main shaft cavity input of two effect drying machines by flash steam recycling system and indirect steam and connected;The discharge gate of one effect drying machine is connected by pressure difference shielding system with two effect drying machines, and the tail gas in two effect dryer cavities is connected with drying tail gas vacuum system;The discharge gate and sealing discharging system connectivity of two effect drying machines.The present invention can realize the recycling of heat, improve thermal source and treat the thermograde of dry material, improve two drying efficiencies for imitating drying machine.
Description
Technical field
The present invention relates to water-containing materials technical field of drying, a kind of height that proposition material saves the energy in the drying process contains
The efficient energy-saving drying system and technique of water material.Especially suitable liquid material and High water cut material, and some are dried
The dry materials of huge energy consumption in journey.It is especially suitable by loss on dryingization to discarded object in environmental protection industry (epi).
Technical background
The method that the drying and dehydrating of material is most basic is that dry material is treated in heating, vaporizes the moisture in material, realizes wet thing
That expects dehydrates.Need to provide heat in the drying process to dry material is treated, make moisture vaporization abjection contained therein, thus it is dry
Dry process huge energy consumption, it is especially prominent for the larger project energy consumption problem of material handling capacity.
Especially in environmental protection industry (epi), minimizing, innoxious, recycling treatment, example are carried out with dry method for discarded object
Such as sludge, high concentration salt solution, drying process energy consumption are excessive, and processing cost is too high, has a strong impact on the economic benefit of enterprise.Simultaneously
Also the social benefit of environmental protection is had a strong impact on.On the other hand, in the drying process, the vapor of vaporization volatilization will be produced material
Exhaust emissions, adds greenhouse air lift discharge, environment is adversely affected.
Current drying technique and equipment have diversified forms, for material in industrial products and industrial process or agricultural byproducts
The problem of drying, energy consumption, less protrudes, but in emerging environmental protection industry (epi), what the problem of drying process energy consumption is reduced showed extremely dashes forward
Go out.In order to save the energy, energy consumption is reduced, people in equipment in a variety of drying processes with being screened, and majority is thought using conduction
Heat drying Technical comparing is saved, and the present invention is on the basis of conduction heating dry technology, using new process, is realized dry
Energy consumption is greatly lowered in dry process.
The content of the invention
To overcome the deficiencies in the prior art, the present invention provides the efficient energy-saving drying system and work of a kind of High water cut material
Skill, can make material reduce energy consumption in drying process, reduce greenhouse gas emission.
For achieving the above object, the present invention adopts the following technical scheme that realization:
A kind of efficient energy-saving drying system of High water cut material, including:One effect drying machine(1), two effect drying machines(2), it is once hot
Source system(3), described effect drying machine(1)For positive pressuring drying machine, two effect drying machines(2)For negative pressure of vacuum drying machine;One effect
Drying machine(1)Main shaft cavity input pass through pipeline and a heat source system(3)Output end is connected;One effect drying machine(1)Chamber
Internal tail gas recycles heat source system by indirect steam(4)Input connection, it is described one effect drying machine(1)Cavity
Filling end passes through indirect steam replenishment system(5)With a heat source system(3)Connection;One effect drying machine(1)Main shaft cavity it is defeated
Go out end and pass through pipeline, hydrophobic station and flash steam recycling system(6)Connection;Flash steam recycling system(6)Sudden strain of a muscle
Bleed steam output end recycles heat source system by pipeline and indirect steam(4)Output end connection, indirect steam reclaim profit
Use heat source system(4)Output end pass through pipeline and two effect drying machines(2)Main shaft cavity input connection;One effect drying machine
(1)Charging aperture pass through pipeline and sealed feed system(8)First output end is connected, an effect drying machine(1)Discharge gate pass through
Pressure difference shielding system(9)With two effect drying machines(2)First charging aperture is connected, two effect drying machines(2)Second charging aperture and sealing
Charging system(8)Second output end is connected;Two effect drying machines(2)Tail gas in cavity is by pipeline with drying tail gas vacuum system
(7)Connection;Two effect drying machines(2)Discharge gate and sealing discharging system(10)Connection.
A kind of efficient energy-saving drying system of High water cut material, a described heat source system(3)It is saturated vapor heat-carrying
Body, or a heat source system(3)It is a thermal source heat-conducting oil system(11)Heat-conducting oil heating thermophore.
A kind of efficient energy-saving drying system of High water cut material, described indirect steam recycles heat source system(4)By
Positioned at an effect drying machine(1)Several dry collectors on top are connected composition with wet scrubber by pipeline.
A kind of efficient energy-saving drying system of High water cut material, described sealed feed system(8)By distribution feed bin and cloth
Expect that spiral is constituted, sealed feed system(8)On be respectively arranged with to the first output end of an effect drying machine charging and dry to two effects
Second output end of dry machine charging, adds for the sealing to aqueous powder material and plaster pasty materials and block filter cake material
Material;
A kind of efficient energy-saving drying system of High water cut material, described sealed feed system(8)Or replace with to liquid material
The sealed feed system of charging(12)It is made up of charge pump, high-order pressure stabilizing tank, pipeline and valve, has charge pump, valve to pass through pipe
Road has charge pump, valve to imitate drying machines to two by high-order voltage stabilizing hopper, pipeline to the first output end of an effect drying machine charging
Second output end of charging.
A kind of efficient energy-saving drying system of High water cut material, described pressure difference shielding system(9)By autocontrol valve and
Batch can is cached to constitute.
A kind of efficient energy-saving drying process of High water cut material, including processing cream pasty state, aqueous powder or filter cake shape are waited to do
The technique of dry material, the technique for handling liquid material to be dried;
A. the technique for handling cream pasty state, aqueous powder or filter cake shape material to be dried, its step is as follows:
1), one effect drying machine charging, by sealed feed system(8)Material to be dried is added, an effect drying machine is entered back into(1)Cavity
It is interior;Sealed feed system (8) is made up of distribution feed bin and cloth spiral, and feeding quantity is realized by automatic control system;Sealing charging
The sealing characteristics of system (8) are to seal to complete by material;No matter charging carries out state or charging halted state, hermetic seal shape
State keeps effective;
2), one effect drying machine heat drying:One effect drying machine(1)The thermal source used is steam, and the steam from boiler passes through one
Secondary heat source stream system(3)Into an effect drying machine(1)Main shaft cavity in, one imitate drying machine(1)After middle carry out heat exchange
Mutually it is changed into condensed water discharge, the condensed water of discharge returns to boiler after draining system;The flash steam produced in hydrophobic process,
Pass through flash steam recycling system(6)After collection, flash steam recycles heat source system with indirect steam again(4)Output
The clean steam at end is converged, and is used as two effect drying machines(2)Thermal source, into two effect drying machines(2)Main shaft cavity in;
3), one effect drying machine(1)Discharge:Pass through an effect drying machine(1)Dried dry material passes through an effect drying machine(1)With
Two effect drying machines(2)The pressure difference shielding system 9 of UNICOM is discharged into two effect drying machines(2);Pressure difference shielding system is by control valve and caching
Batch can is constituted;The pressure difference shielding system controls control valve by control system, has both ensured an effect drying machine(1)Dried dry material
Discharge, and ensure simultaneously to an effect drying machine(1)With two effect drying machines(2)Pressure difference isolation is carried out, keeps one to imitate drying machine(1)
Direct draught is run and two effect drying machines(2)Run under negative pressure;
4)One effect drying machine(1)Exhaust emissions, one effect drying machine(1)Tail gas discharge be the dust-laden steam with pressure, lead to
Cross indirect steam and recycle heat source system(4)Come what is completed, two effect drying machines are used as after dust separation(2)Thermal source;
5)Two effect drying machines(2)Charging:One is to add material to be dried by sealed feed system (8), enters back into two effect dryings
Machine(2)In cavity;Sealed feed system (8) is made up of distribution feed bin and cloth spiral, and feeding quantity is realized by automatic control system;
Its sealing characteristics is to seal to complete by material;No matter charging carries out state or charging halted state, and hermetic seal state is protected
Hold effectively;Two be by an effect drying machine(1)With two effect drying machines(2)The pressure difference shielding system of UNICOM adds two and imitates drying machine(2);
6), two effect drying machine heat dryings:Two effect drying machines(2)First thermal source used is that indirect steam recycles thermal source
System(4)The clean steam with pressure of processing;Second thermal source used is by an effect drying machine(1)Steam condensation
The flash steam that water comes out by shwoot is through hydrophobic flash steam recycling system(6)Flash steam after collection, is used as two
Imitate drying machine(2)Thermal source feeding two imitates drying machine(2);Described indirect steam recycles heat source system(4)By dry dust removal
Device, wet scrubber and pipeline composition;I.e. after dry collector one-time dedusting into wet scrubber final dusting into
For the clean steam with pressure;
The 3rd thermal source used comes from indirect steam replenishment system(5), when an effect drying machine(1)Produced is secondary
Dust-laden steam and flash steam recycling system(6)The steam of recycling, is not enough to drive two to imitate drying machine(2)When, lead to
Cross indirect steam replenishment system(5)Supplement;
Indirect steam replenishment system(5)It is that will heat a heat source system(3)Steam source be passed through an effect drying machine(1)Shell
In vivo, it was changed into low pressure vapours, and added an effect drying machine(1)Tail gas discharge rate;Simultaneously to an effect drying machine(1)Have auxiliary
Desiccation is helped, and has superheat protecting function to indirect steam recycling system, is unlikely to dust-laden steam in indirect steam
Condense and block in deduster and pipeline in recycling system, supplement the pressure of steam by pressure maintaining valve control;
7), two effect drying machines(2)Discharge:Two effect drying machines(2)It is negative pressure drying, two imitates drying machine in the drying process(2)
Pressure in housing is less than environment atmospheric pressure;Two effect drying machines(2)Dried material is by sealing discharging system (10) discharge;
Sealing discharging system (10) is made up of the gentle material stocking pipe of autocontrol valve, and its effect is two effect drying machines(2)Dried material
Material is discharged, but sealing discharging system (10) is isolated with ambient air all the time, keeps two to imitate drying machine(2)Negative pressure state;Two
Imitate drying machine(2)Sealing discharging system (10) by control system control;
8), two effect drying machines(2)Exhaust emissions:Two effect drying machines(2)The tail gas of discharge is negative pressure dust-laden steam, two effect dryings
Machine(2)The vent gas treatment of discharge is by drying tail gas vacuum system(7)Complete, dry tail gas vacuum system(7)Removed by wet type
The dedusting of dirt device and condenser composition;I.e. by entering condenser after wet scrubber dedusting, after volatilization steam condensation, fixed gas
There is vacuum pump set extraction, condenser arranges condensed water and is discharged into sewage disposal system;
Two effect drying machines are set up and maintained by tail gas vacuum system(2)Dryings are imitated in interior vacuum state, reduction and holding two
Machine(2)The volatilization temperature of interior material hygroscopic water;So that two effect drying machines(2)Thermal source and treat that dry material keeps larger temperature ladder
Degree, improves two and imitates drying machine(2)Drying efficiency;
Two described effect drying machines(2)Thermal source used is by an effect drying machine(1)Produced indirect steam is provided, and realizes saving
The purpose of the energy;
B. the technique for handling liquid material to be dried,
One effect drying machine(1)With two effect drying machines(2)Thermal source, discharge, exhaust emissions with A. processing cream pasty state, aqueous powder or
The technique of filter cake shape material to be dried;When it is liquid material to handle material to be dried, its step is as follows:
1), one effect drying machine(1)Charging:One effect drying machine(1)For positive pressuring drying, liquid treats that dry material passes through pipe by charge pump
Road and valve are directly added into, and feed pressure and flow are by the valve regulated of sealed feed system, and feeding quantity is by automatic control system
Control;
2), two effect drying machines(2)Charging:Two effect drying machines(2)For negative pressure drying, it is high-order that liquid treats that material is added by charge pump
Pressure stabilizing tank, high-order pressure stabilizing tank keeps stable material position pressure to treat that dry material adds two and imitates drying machine(2), keep two to imitate drying machine
(2)The stabilization of feed pressure and flow;Feeding quantity is by automatic control system control;Add liquid object excessive in high-order pressure stabilizing tank
Material returns to storage tank by overflow pipe.
3), charging carry out state or charging halted state, sealed feed system(12)One is all kept to imitate drying machine(1)'s
Barotropic state is run and two effect drying machines(2)Negative pressure state is run;
So sealed feed system(12)It is made up of charge pump, high-order pressure stabilizing tank, pipeline and valve, and due to an effect drying machine
(1)Positive pressuring drying, two effect drying machines(2)For negative pressure drying, feed pressure is also variant.
A kind of efficient energy-saving drying process of High water cut material, it is the heat-carrying that heat-conducting oil furnace is supplied to dry used thermal source
Conduction oil, the technique for including processing cream pasty state, aqueous powder or filter cake shape material to be dried, handles the work of liquid material to be dried
Skill;
A. the thermal source that processing cream pasty state, aqueous powder or filter cake shape material to be dried are used is the technique of conduction oil, its step
It is as follows:
1), one effect drying machine charging, by sealed feed system(8)Add material to be dried;
2), one effect drying machine heat drying:One effect drying machine(1)Heat-carrying conduction oil of the thermal source of use from heat-conducting oil furnace, warp
Thermal source heat-conducting oil system (11) enters one and imitates drying machine(1)Main shaft cavity in, one imitate drying machine(1)In with treat dry
Material discharged after heat exchange, and the conduction oil after heat exchange cooling returns to heat-conducting oil furnace heat temperature raising again;Without other used heat row
Put;
3), one effect drying machine(1)Discharge:Pass through an effect drying machine(1)Dried dry material passes through an effect drying machine(1)With
Two effect drying machines(2)The pressure difference shielding system 9 of UNICOM is discharged into two effect drying machines(2);Both an effect drying machine had been ensured(1)It is dried
Dry material is discharged, and is ensured simultaneously to an effect drying machine(1)With two effect drying machines(2)Pressure difference isolation is carried out, keeps one to imitate drying
Machine(1)Operation under positive pressure and two effect drying machines(2)Run under negative pressure;
4)One effect drying machine(1)Exhaust emissions, one effect drying machine(1)Tail gas discharge be the dust-laden steam with pressure, lead to
Cross indirect steam and recycle heat source system(4)Come what is completed, two effect drying machines are used as after dust separation(2)Thermal source;
5)Two effect drying machines(2)Charging:One is to add material to be dried by sealed feed system (8), enters back into two effect dryings
Machine(2)In cavity;Two be by an effect drying machine(1)With two effect drying machines(2)The pressure difference shielding system of UNICOM adds two and imitates drying
Machine(2);
6), two effect drying machines(2)The thermal source of heat drying:It is an effect drying machine(1)The tail gas of discharge, an effect drying machine(1)Row
The tail gas gone out recycles heat source system by indirect steam(4)The clean steam with pressure after purification enters two effect dryings
Machine(2), with two effect drying machines(2)In be mutually changed into condensed water after after dry material heat exchange and discharged by draining system;
7), two effect drying machines(2)Discharge:Two effect drying machines(2)It is negative pressure drying, two imitates drying machine in the drying process(2)
Pressure in housing is less than environment atmospheric pressure;Two effect drying machines(2)Dried material is by sealing discharging system (10) discharge;
8), two effect drying machines(2)Exhaust emissions:Two effect drying machines(2)The tail gas of discharge is negative pressure dust-laden steam, two effect dryings
Machine(2)The vent gas treatment of discharge is by drying tail gas vacuum system(7)Complete, set up and maintain by tail gas vacuum system
Two effect drying machines(2)Drying machines are imitated in interior vacuum state, reduction and holding two(2)The volatilization temperature of interior material hygroscopic water;So that
Two effect drying machines(2)Thermal source and treat that dry material keeps larger thermograde, improve two and imitate drying machines(2)Drying efficiency;
B. the thermal source that is used of processing liquid material to be dried is the technique of conduction oil, and its step is as follows:
One effect drying machine(1)With two effect drying machines(2)Thermal source, discharge, exhaust emissions with A. processing cream pasty state, aqueous powder or
The technique of filter cake shape material to be dried;When it is liquid material to handle material to be dried, its step is as follows:
1), one effect drying machine(1)Charging:One effect drying machine(1)For positive pressuring drying, liquid treats that dry material passes through pipe by charge pump
Road and valve are directly added into, and feed pressure and flow are by the valve regulated of sealed feed system, and feeding quantity is by automatic control system
Control;
2), two effect drying machines(2)Charging:Two effect drying machines(2)For negative pressure drying, it is high-order that liquid treats that material is added by charge pump
Pressure stabilizing tank, high-order pressure stabilizing tank keeps stable material position pressure to treat that dry material adds two and imitates drying machine(2), keep two to imitate drying machine
(2)The stabilization of feed pressure and flow;Feeding quantity is by automatic control system control;Add liquid object excessive in high-order pressure stabilizing tank
Material returns to storage tank by overflow pipe.
3), charging carry out state or charging halted state, sealed feed system(12)One is all kept to imitate drying machine(1)'s
Barotropic state is run and two effect drying machines(2)Negative pressure state is run;
So sealed feed system(12)It is made up of charge pump, high-order pressure stabilizing tank, pipeline and valve, and due to an effect drying machine
(1)Positive pressuring drying, two effect drying machines(2)For negative pressure drying, feed pressure is also variant.
Due to using technical scheme as described above, the present invention has following superiority:
The efficient energy-saving drying system and technique of a kind of High water cut material, the effect drying machine used exist for the purpose of positive pressuring drying
There is certain steam pressure in the indirect steam discharged, two thermals source for imitating drying machines can be used as.Two effect drying machines are negative for vacuum
Press dry dry purpose to be to improve thermal source and treat the thermograde of dry material, improve two drying efficiencies for imitating drying machine.Use
Heat source system can be steam thermophore, can also be heat-conducting oil heating thermophore.In the heat source system of steam thermophore,
Boiler is returned after drain valve through the steam condensate (SC) of an effect drying machine, heat recovery and desalination Water Sproading is realized.Institute's shwoot
Flash steam out enters indirect steam through flash steam recycling system and recycles heat source system as two effect dryings
The thermal source of machine.In heat transfer oil heat carrier heat source system, the conduction oil of heat-carrying returns to heat-conducting oil furnace again after an effect drying machine heat exchange,
Realize the recycling of heat.
The indirect steam recycling system of use is the dust-laden steam for having certain pressure for being discharged an effect drying machine
It is used after dry collector and wet scrubber dust separation as the thermal source of two effect drying machines.For an effect drying
The heat source system of machine is the case of steam thermophore heat source system, and its flash steam is incorporated to by flash steam recycling system
Indirect steam recycling system.
When the secondary dust-laden steam produced by an effect drying machine is not enough to drive two effect drying machines, indirect steam can be passed through
Replenishment system is supplemented.Indirect steam replenishment system is will to heat a heat source stream for imitating drying machine to be passed through an effect drying machine
In housing, it was changed into low pressure vapours, and had auxiliary desiccation to an effect drying machine, while to indirect steam recycling system
There is superheat protecting function, be unlikely to condense in deduster and pipeline of the dust-laden steam in indirect steam recycling system and block up
Plug, the pressure of the supplement steam of use is by pressure maintaining valve control.
The vent gas treatment of the two effect drying machine discharges used is completed by drying tail gas vacuum system, passes through wet dust removal
Enter condenser after device dedusting, after volatilization steam condensation, fixed gas is drawn by vacuum pump set.Tail gas vacuum system is set up and tieed up
The vacuum state in two effect drying machines, reduction and the volatilization temperatures for keeping material hygroscopic water in two effect drying machines are held.So that two
Imitate the thermal source of drying machine and treat that dry material keeps larger thermograde, improve two drying efficiencies for imitating drying machine.
The sealed feed system of use(Aqueous powder material, plaster pasty materials, liquid material), be to have been sealed by material
Into.No matter charging carries out state or charging halted state, and its sealing state keeps effective.For aqueous powder material and cream
Pasty material and block filter cake material, sealed feed system are made up of distribution feed bin and cloth spiral.An effect is separately added into do
Dry machine and two effect drying machines, the control of feeding quantity are completed by automatic control system.
For liquid material, charging system is made up of charge pump, high-order voltage stabilizing hopper, pipeline and valve, is separately added into one
Drying machine and two effect drying machines are imitated, the control of feeding quantity is completed by automatic control system.
The pressure difference shielding system of use is made up of the gentle material stocking pipe of autocontrol valve, due to the dry material of an effect drying machine
Temperature be higher than temperature of charge in close drying machine, be loaded with certain heat, have auxiliary dry materials in two effect drying machines
Dry effect and heat energy utilization effect.So a dried heat-carrying dry material of effect drying machine will enter in two effect drying machines.One effect
The effect of the pressure difference shielding system of drying machine and two effect drying machines is that the dried heat-carrying dry material of an effect drying machine can enter
In two effect drying machines, but pressure difference isolation is carried out to an effect drying machine and two effect drying machines simultaneously, keep one to imitate drying machine and two effects
Drying machine is run under respective pressure field.The pressure difference shielding system of one effect drying machine and two effect drying machines is by control system control
System.
The two effect dried materials of drying machine used are by sealing discharging system discharge, by the gentle material stocking pipe of autocontrol valve
Constitute, it is the dried material material discharge of two effect drying machines that it, which is acted on, but keeps two pressure states for imitating drying machine simultaneously.
Brief description of the drawings
Thermal source of the present invention can be conduction oil or steam, and the state for treating dry material adapted to can be liquid, cream pasty state, filter cake
Shape, aqueous powder.Drawings described below explanation is made with the dosing form for treating dry material state according to heat resource form:
Fig. 1, thermal source are steam, and material is cream pasty state, aqueous powder, filter cake shape technological process;
Fig. 2, thermal source are steam, and material is liquid process flow
Fig. 3, thermal source are conduction oil, and material is cream pasty state, aqueous powder, filter cake shape technological process;
Fig. 4, thermal source are conduction oil, and material is liquid process flow.
In figure:1st, an effect drying machine;2nd, two effect drying machine;3rd, a heat source stream system;4th, indirect steam is recycled
Heat source system;5th, indirect steam replenishment system;6th, flash steam recycling system;7th, tail gas vacuum system is dried;8th, seal
Charging system(Aqueous powder material, plaster pasty materials, filter cake shape material)9th, one effect drying machine and two effect drying machines pressure difference every
From system;10th, sealing discharging system;11st, a thermal source heat-conducting oil system;12nd, sealed feed system (liquid material).
Embodiment
Embodiment one
Technological process shown in Fig. 1, material state to be dried is cream pasty state, aqueous powder or filter cake shape, and such as moisture content is 80%
Municipal sludge, dry the steam that used thermal source is boiler supplying.
The present embodiment one imitates drying machine from one(1)With two effect drying machines(2)Charging, thermal source, discharge, in terms of exhaust emissions
State the logical relation and energy-saving principle of technological process shown in Fig. 1.
One effect drying machine(1)Charging:
One effect drying machine(1)By sealed feed system(10)Material to be dried is added, sealed feed system (10) is by distribution feed bin
Constituted with cloth spiral, feeding quantity is realized by automatic control system.Its sealing characteristics is to seal to complete by material.No matter plus
Expect carry out state or charging halted state, hermetic seal state keeps effective.
One effect drying machine(1)Thermal source:
One effect drying machine(1)Thermal source be steam, the steam from boiler passes through a heat source stream system(3)It is dry into an effect
Dry machine(1), drying machine is imitated one(1)Mutually it is changed into condensed water discharge after middle carry out heat exchange, the condensed water of discharge is through draining system
After return to boiler.Certain flash steam is had in hydrophobic process, the present invention passes through flash steam recycling system(6)Receive
Indirect steam is sent into after collection and recycles heat source system(4), it is used as two effect drying machines(2)Thermal source.
One effect drying machine(1)Discharge:
One effect drying machine(1)Dried dry material discharge is by an effect drying machine(1)With two effect drying machines(2)Pressure difference every
Two effect drying machines are discharged into from system(2), an effect drying machine(1)With two effect drying machines(2)Pressure difference shielding system by automatically controlling
The gentle material stock tank of valve is constituted.One effect drying machine(1)With two effect drying machines(2)Pressure difference shielding system by automatic control system control
System.Both an effect drying machine had been ensured(1)Dried dry material discharge, and ensure simultaneously to an effect drying machine(1)With two effect dryings
Machine(2)Pressure difference isolation is carried out, keeps one to imitate drying machine(1)With two effect drying machines(2)Run under respective pressure field.
Due to an effect drying machine(1)Dry material temperature higher than two effect drying machines(2)In temperature of charge, be loaded with one
Fixed heat, to two effect drying machines(2)In material have auxiliary desiccation and heat energy utilization effect.So an effect drying machine
(1)Dried heat-carrying dry material will enter two effect drying machines(2)In, it is also the behave that the present invention realizes energy-conservation.
One effect drying machine(1)Exhaust emissions:
One effect drying machine(1)Tail gas be the dust-laden steam with certain pressure, two effect drying machines are used as after dust separation
(2)Thermal source.Indirect steam is recycled, and realizes the purpose of energy-conservation of the invention.
One effect drying machine(1)Tail gas discharge the dust-laden steam with certain pressure be to be recycled by indirect steam
Heat source system(4)Come what is completed, indirect steam recycles heat source system(4)By dry collector, wet scrubber and pipeline
Composition.
One effect drying machine(1)Tail gas discharge the dust-laden steam with certain pressure by dry collector one-time dedusting
Entering wet scrubber final dusting afterwards turns into the clean steam with certain pressure.It is used as two effect drying machines(2)Thermal source is sent into
Two effect drying machines(2).
Two effect drying machines(2)Charging:
Two effect drying machines(2)Material to be dried is added by sealed feed system (10), sealed feed system (10) is by distribution feed bin
Constituted with cloth spiral, feeding quantity is realized by automatic control system.Its sealing characteristics is to seal to complete by material.No matter plus
Expect carry out state or charging halted state, hermetic seal state keeps effective.
Two effect drying machines(2)Another part charging before to have addressed be an effect drying machine(1)Dried material passes through one
Imitate drying machine(1)With two effect drying machines(2)Pressure difference shielding system add two imitate drying machines(2).
Two effect drying machines(2)Thermal source:
It is preceding to have addressed two effect drying machines(2)Thermal source be by one effect drying machine(1)Tail gas after dust removal process be used as two effect
Drying machine(2)Thermal source, this is two effect drying machines(2)Thermal source main source, but also two source.
Two effect drying machines(2)Second of thermal source come from flash steam recycling system(6), through an effect
Drying machine(1)Steam condensate (SC) boiler is returned after drain valve, realize heat recovery and desalination Water Sproading.Institute's shwoot comes out
Flash steam through flash steam recycling system(6)Heat source system is recycled into indirect steam(4)It is dry as two effects
Dry machine(2)Thermal source.
Two effect drying machines(2)The 3rd of thermal source come from indirect steam replenishment system(5), when an effect drying machine
(1)Produced secondary dust-laden steam and flash steam recycling system(6)The steam of recycling is not enough to drive two effects
Drying machine(2)When, indirect steam replenishment system can be passed through(5)Supplement.Indirect steam replenishment system(5)It is that will heat a thermal source
System(3)A heat source stream be passed through an effect drying machine(1)Housing in, be changed into low pressure vapours, add an effect do
Dry machine(1)Tail gas discharge rate;Simultaneously to an effect drying machine(1)There is auxiliary desiccation, and indirect steam is recycled
System has superheat protecting function, is unlikely to condense in deduster and pipeline of the dust-laden steam in indirect steam recycling system
Block.
The pressure of steam is supplemented by pressure maintaining valve control.
Two effect drying machines(2)Discharge:
Two effect drying machines(2)It is negative pressure drying, two imitates drying machine in the drying process(2)Pressure in housing is less than ambient air
Pressure.Two effect drying machines(2)Dried material is by sealing discharging system (10) discharge.By the gentle material stocking pipe structure of autocontrol valve
Into its effect is two effect drying machines(2)Dried material material discharge, but isolate the effect drying of holding two with ambient air all the time
Machine(2)Pressure state.
Two effect drying machines(2)Sealing discharging system (10) by automatic control system control.
Two effect drying machines(2)Exhaust emissions:
Two effect drying machines(2)The tail gas of discharge is negative pressure dust-laden steam, two effect drying machines(2)The vent gas treatment of discharge is by drying
Tail gas vacuum system(7)Complete, by entering condenser after wet scrubber dedusting, after volatilization steam condensation, fixed gas
There is vacuum pump set extraction.Condenser arranges condensed water and is discharged into sewage disposal system.
Two effect drying machines are set up and maintained to tail gas vacuum system(2)Dryings are imitated in interior vacuum state, reduction and holding two
Machine(2)The volatilization temperature of interior material hygroscopic water.So that two effect drying machines(2)Thermal source and treat that dry material keeps larger temperature ladder
Degree, improves two and imitates drying machine(2)Drying efficiency.
Embodiment one illustrates the two effect drying machines of the present invention(2)Thermal source used is by an effect drying machine(1)Produced two
Secondary steam is provided, and realizes the purpose for saving the energy.
Embodiment one also illustrates the process conditions for realizing that energy-conservation purpose should possess.
Embodiment two
Technological process shown in Fig. 2, material state to be dried is liquid, after obtain solid material, such as moisture content is 80% height
Concentration salt solution.One effect drying machine(1)The thermal source used for boiler supplying steam.
Embodiment two imitates drying machine from one(1)With two effect drying machines(2)Charging, thermal source, discharge, old in terms of exhaust emissions
State the logical relation and energy-saving principle of technological process shown in Fig. 2.One effect drying machine of embodiment two(1)With two effect drying machines(2)
Thermal source, discharge, exhaust emissions and embodiment one it is just the same, repeat no more.Only charging has difference with embodiment one.Embodiment
One thermal source, discharge, process system described in exhaust emissions belong to present disclosure together applied to embodiment two.
Because embodiment two treats that dry material state is liquid, so sealed feed system (liquid material)(12)There is charging
Pump, high-order pressure stabilizing tank, pipeline and valve composition.And due to an effect drying machine(1)Positive pressuring drying, two effect drying machines(2)It is negative
Press dry dry, feed pressure is also variant.
One effect drying machine(1)Charging:
One effect drying machine(1)For positive pressuring drying, liquid treats that dry material is directly added into by charge pump by pipeline and valve, charging pressure
Power and flow by sealed feed system valve regulated.Feeding quantity is by automatic control system control.
Two effect drying machines(2)Charging:
Two effect drying machines(2)For negative pressure drying, liquid treats that material adds high-order pressure stabilizing tank by charge pump, and high-order pressure stabilizing tank keeps steady
Fixed material position pressure will treat that dry material adds two and imitates drying machine(2), keep two to imitate drying machine(2)Feed pressure and flow it is steady
It is fixed.Feeding quantity is by automatic control system control.Add liquid material excessive in high-order pressure stabilizing tank and storage tank is returned to by overflow pipe.
In charging carry out state or charging halted state, sealed feed system(12)One is all kept to imitate drying machine(1)Just
Pressure condition is run and two effect drying machines(2)Negative pressure state is run.
Embodiment three
Technological process shown in Fig. 3, material state to be dried is cream pasty state, aqueous powder or filter cake shape, and such as moisture content is 80%
Municipal sludge, it is the heat-carrying conduction oil that heat-conducting oil furnace is supplied to dry used thermal source.
The present embodiment imitates drying machine from one(1)With two effect drying machines(2)Charging, thermal source, discharge, old in terms of exhaust emissions
State the logical relation and energy-saving principle of technological process shown in Fig. 3.One effect drying machine of embodiment three(1)With two effect drying machines(2)
Charging, discharge, exhaust emissions and embodiment one it is just the same, repeat no more.Only thermal source has difference with embodiment one.Embodiment
One charging, discharge, process system described in exhaust emissions belong to present disclosure together applied to embodiment three.
Three heat source systems of embodiment use heat-conducting oil heating system:
One effect drying machine(1)Thermal source:
Heat-carrying conduction oil from heat-conducting oil furnace enters one through a thermal source heat-conducting oil system (11) and imitates drying machine(1), in an effect
Drying machine(1)In with after dry material carry out heat exchange after discharge, heat exchange cooling after conduction oil return to again heat-conducting oil furnace heat
Heating.Without other waste heat discharges.
Two effect drying machines(2)Thermal source:
Embodiment three is similar with embodiment one, two effect drying machines(2)Thermal source is an effect drying machine(1)The tail gas of discharge a, effect is dry
Dry machine(1)The tail gas of discharge recycles heat source system purification by indirect steam(4)Enter two afterwards and imitate drying machine(2), with two
Imitate drying machine(2)In be mutually changed into condensed water after after dry material heat exchange and discharged by draining system.
Two effect drying machine unlike embodiment three and embodiment one(2)Heat source system does not contain indirect steam replenishment system
(5)With flash steam recycling system(6).
Example IV
Technological process shown in Fig. 4, material state to be dried is liquid, and solid material is obtained after drying, and such as moisture content is 80%
High concentration salt solution.It is the heat-carrying conduction oil that heat-conducting oil furnace is supplied to dry used thermal source.It is to treat dry material state and thermal source
Another process combination form of form.
Example IV imitates drying machine from one(1)With two effect drying machines(2)Charging, thermal source, discharge, old in terms of exhaust emissions
State the logical relation and energy-saving principle of technological process shown in Fig. 4.
One effect drying machine(1)With two effect drying machines(2)Charging:
Example IV is consistent with the material state handled by embodiment two, an effect drying machine(1)With two effect drying machines(2)Charging
Form is identical with content described in embodiment two.
One effect drying machine(1)With two effect drying machines(2)Thermal source:
Thermal source of example IV and embodiment three is all conduction oil, an effect drying machine(1)Thermal source use form and implementation
Example embodiment three is identical.Two effect drying machines(2)The energy saving form of thermal source and embodiment three it is identical.
One effect drying machine(1)With two effect drying machines(2)Discharge:
One effect drying machine of example IV and embodiment one(1)With two effect drying machines(2)Discharge form it is identical.
One effect drying machine(1)With two effect drying machines(2)Exhaust emissions:
One effect drying machine of example IV and embodiment one(1)With two effect drying machines(2)Exhaust emissions form it is identical.
The present invention realizes effective profit of indirect steam and used heat by rational technological process and required process conditions
With, realize variform material drying it is energy-saving.To the present invention reduction technical requirements carry out simple copy, split or
Combination belongs to the interest field of the present invention.
Claims (8)
1. a kind of efficient energy-saving drying system of High water cut material, including:One effect drying machine(1), two effect drying machines(2), once
Heat source system(3), it is characterized in that:A described effect drying machine(1)For positive pressuring drying machine, two effect drying machines(2)For negative pressure of vacuum
Drying machine;One effect drying machine(1)Main shaft cavity input pass through pipeline and a heat source system(3)Output end is connected;One effect
Drying machine(1)Tail gas in cavity recycles heat source system by indirect steam(4)Input connection, it is described one effect drying
Machine(1)The filling end of cavity passes through indirect steam replenishment system(5)With a heat source system(3)Connection;One effect drying machine(1)'s
Main shaft cavity output end passes through pipeline, hydrophobic station and flash steam recycling system(6)Connection;Flash steam recycles system
System(6)Flash steam output end pass through pipeline and indirect steam and recycle heat source system(4)Output end connection, it is secondary steam
Vapour recycles heat source system(4)Output end pass through pipeline and two effect drying machines(2)Main shaft cavity input connection;One effect
Drying machine(1)Charging aperture pass through pipeline and sealed feed system(8)First output end is connected, an effect drying machine(1)Discharge
Mouth passes through pressure difference shielding system(9)With two effect drying machines(2)First charging aperture is connected, two effect drying machines(2)Second charging aperture
With sealed feed system(8)Second output end is connected;Two effect drying machines(2)Tail gas in cavity is true with drying tail gas by pipeline
Empty set is united(7)Connection;Two effect drying machines(2)Discharge gate and sealing discharging system(10)Connection.
2. a kind of efficient energy-saving drying system of High water cut material according to claim 1, it is characterized in that:It is described once
Heat source system(3)It is saturated vapor thermophore, or a heat source system(3)It is a thermal source heat-conducting oil system(11)Conduction oil
Heat thermophore.
3. a kind of efficient energy-saving drying system of High water cut material according to claim 1, it is characterized in that:Described is secondary
Steam Recovery utilizes heat source system(4)By positioned at an effect drying machine(1)Several dry collectors on top by pipeline with it is wet
Formula deduster connection composition.
4. a kind of efficient energy-saving drying system of High water cut material according to claim 1, it is characterized in that:Described sealing
Charging system(8)It is made up of distribution feed bin and cloth spiral, sealed feed system(8)On be respectively arranged with to one effect drying machine add
First output end of material and the second output ends to two effect drying machines chargings, for aqueous powder material and plaster pasty materials with
And the sealing charging of block filter cake material.
5. a kind of efficient energy-saving drying system of High water cut material according to claim 1, it is characterized in that:Described sealing
Charging system(8)Or replace with the sealed feed system fed to liquid material(12)By charge pump, high-order pressure stabilizing tank, pipeline and
Valve is constituted, the first output end for having charge pump, valve to be fed by pipeline to an effect drying machine, has charge pump, valve to pass through
The second output end that high-order voltage stabilizing hopper, pipeline feed to two effect drying machines.
6. a kind of efficient energy-saving drying system of High water cut material according to claim 1, it is characterized in that:Described pressure difference
Shielding system(9)It is made up of the gentle material stock tank of autocontrol valve.
7. a kind of efficient energy-saving drying process of High water cut material, it is characterized in that:Including processing cream pasty state, aqueous powder or filter cake
The technique of shape material to be dried, the technique for handling liquid material to be dried;
A. the technique for handling cream pasty state, aqueous powder or filter cake shape material to be dried, its step is as follows:
1), one effect drying machine charging, by sealed feed system(8)Material to be dried is added, an effect drying machine is entered back into(1)Cavity
It is interior;Sealed feed system (8) is made up of distribution feed bin and cloth spiral, and feeding quantity is realized by automatic control system;Sealing charging
The sealing characteristics of system (8) are to seal to complete by material;No matter charging carries out state or charging halted state, hermetic seal shape
State keeps effective;
2), one effect drying machine heat drying:One effect drying machine(1)The thermal source used is steam, and the steam from boiler passes through one
Secondary heat source stream system(3)Into an effect drying machine(1)Main shaft cavity in, one imitate drying machine(1)After middle carry out heat exchange
Mutually it is changed into condensed water discharge, the condensed water of discharge returns to boiler after draining system;The flash steam produced in hydrophobic process,
Pass through flash steam recycling system(6)After collection, flash steam recycles heat source system with indirect steam again(4)Output
The clean steam at end is converged, and is used as two effect drying machines(2)Thermal source, into two effect drying machines(2)Main shaft cavity in;
3), one effect drying machine(1)Discharge:Pass through an effect drying machine(1)Dried dry material passes through an effect drying machine(1)With
Two effect drying machines(2)The pressure difference shielding system 9 of UNICOM is discharged into two effect drying machines(2);Pressure difference shielding system is by control valve and caching
Batch can is constituted;The pressure difference shielding system controls control valve by control system, has both ensured an effect drying machine(1)Dried dry material
Discharge, and ensure simultaneously to an effect drying machine(1)With two effect drying machines(2)Pressure difference isolation is carried out, keeps one to imitate drying machine(1)
Direct draught is run and two effect drying machines(2)Run under negative pressure;
4)One effect drying machine(1)Exhaust emissions, one effect drying machine(1)Tail gas discharge be the dust-laden steam with pressure, lead to
Cross indirect steam and recycle heat source system(4)Come what is completed, two effect drying machines are used as after dust separation(2)Thermal source;
5)Two effect drying machines(2)Charging:One is to add material to be dried by sealed feed system (8), enters back into two effect dryings
Machine(2)In cavity;Sealed feed system (8) is made up of distribution feed bin and cloth spiral, and feeding quantity is realized by automatic control system;
Its sealing characteristics is to seal to complete by material;No matter charging carries out state or charging halted state, and hermetic seal state is protected
Hold effectively;Two be by an effect drying machine(1)With two effect drying machines(2)The pressure difference shielding system of UNICOM adds two and imitates drying machine(2);
6), two effect drying machine heat dryings:Two effect drying machines(2)First thermal source used is that indirect steam recycles thermal source
System(4)The clean steam with pressure of processing;Second thermal source used is by an effect drying machine(1)Steam condensation
The flash steam that water comes out by shwoot is through hydrophobic flash steam recycling system(6)Flash steam after collection, is used as two
Imitate drying machine(2)Thermal source feeding two imitates drying machine(2);Described indirect steam recycles heat source system(4)By dry dust removal
Device, wet scrubber and pipeline composition;I.e. after dry collector one-time dedusting into wet scrubber final dusting into
For the clean steam with pressure;
The 3rd thermal source used comes from indirect steam replenishment system(5), when an effect drying machine(1)Produced is secondary
Dust-laden steam and flash steam recycling system(6)The steam of recycling, is not enough to drive two to imitate drying machine(2)When, lead to
Cross indirect steam replenishment system(5)Supplement;
Indirect steam replenishment system(5)It is that will heat a heat source system(3)Steam source be passed through an effect drying machine(1)Shell
In vivo, it was changed into low pressure vapours, and added an effect drying machine(1)Tail gas discharge rate;Simultaneously to an effect drying machine(1)Have auxiliary
Desiccation is helped, and has superheat protecting function to indirect steam recycling system, is unlikely to dust-laden steam in indirect steam
Condense and block in deduster and pipeline in recycling system, supplement the pressure of steam by pressure maintaining valve control;
7), two effect drying machines(2)Discharge:Two effect drying machines(2)It is negative pressure drying, two imitates drying machine in the drying process(2)
Pressure in housing is less than environment atmospheric pressure;Two effect drying machines(2)Dried material is by sealing discharging system (10) discharge;
Sealing discharging system (10) is made up of the gentle material stocking pipe of autocontrol valve, and its effect is two effect drying machines(2)Dried material
Material is discharged, but sealing discharging system (10) is isolated with ambient air all the time, keeps two to imitate drying machine(2)Negative pressure state;Two
Imitate drying machine(2)Sealing discharging system (10) by control system control;
8), two effect drying machines(2)Exhaust emissions:Two effect drying machines(2)The tail gas of discharge is negative pressure dust-laden steam, two effect dryings
Machine(2)The vent gas treatment of discharge is by drying tail gas vacuum system(7)Complete, dry tail gas vacuum system(7)Removed by wet type
The dedusting of dirt device and condenser composition;I.e. by entering condenser after wet scrubber dedusting, after volatilization steam condensation, fixed gas
There is vacuum pump set extraction, condenser arranges condensed water and is discharged into sewage disposal system;
Two effect drying machines are set up and maintained by tail gas vacuum system(2)Dryings are imitated in interior vacuum state, reduction and holding two
Machine(2)The volatilization temperature of interior material hygroscopic water;So that two effect drying machines(2)Thermal source and treat that dry material keeps larger temperature ladder
Degree, improves two and imitates drying machine(2)Drying efficiency;
Two described effect drying machines(2)Thermal source used is by an effect drying machine(1)Produced indirect steam is provided, and realizes saving
The purpose of the energy;
B. the technique for handling liquid material to be dried,
One effect drying machine(1)With two effect drying machines(2)Thermal source, discharge, exhaust emissions with A. processing cream pasty state, aqueous powder or
The technique of filter cake shape material to be dried;When it is liquid material to handle material to be dried, its step is as follows:
1), one effect drying machine(1)Charging:One effect drying machine(1)For positive pressuring drying, liquid treats that dry material passes through pipe by charge pump
Road and valve are directly added into, and feed pressure and flow are by the valve regulated of sealed feed system, and feeding quantity is by automatic control system
Control;
2), two effect drying machines(2)Charging:Two effect drying machines(2)For negative pressure drying, it is high-order that liquid treats that material is added by charge pump
Pressure stabilizing tank, high-order pressure stabilizing tank keeps stable material position pressure to treat that dry material adds two and imitates drying machine(2), keep two to imitate drying machine
(2)The stabilization of feed pressure and flow;Feeding quantity is by automatic control system control;Add liquid object excessive in high-order pressure stabilizing tank
Material returns to storage tank by overflow pipe;
3), charging carry out state or charging halted state, sealed feed system(12)One is all kept to imitate drying machine(1)Malleation
State is run and two effect drying machines(2)Negative pressure state is run;
So sealed feed system(12)It is made up of charge pump, high-order pressure stabilizing tank, pipeline and valve, and due to an effect drying machine
(1)Positive pressuring drying, two effect drying machines(2)For negative pressure drying, feed pressure is also variant.
8. a kind of efficient energy-saving drying process of High water cut material according to claim 1, it is characterized in that:Drying is used
Thermal source be heat-carrying conduction oil that heat-conducting oil furnace is supplied, including processing cream pasty state, aqueous powder or filter cake shape material to be dried
Technique, the technique for handling liquid material to be dried;
A. the thermal source that processing cream pasty state, aqueous powder or filter cake shape material to be dried are used is the technique of conduction oil, its step
It is as follows:
1), one effect drying machine charging, by sealed feed system(8)Add material to be dried;
2), one effect drying machine heat drying:One effect drying machine(1)Heat-carrying conduction oil of the thermal source of use from heat-conducting oil furnace, warp
Thermal source heat-conducting oil system (11) enters one and imitates drying machine(1)Main shaft cavity in, one imitate drying machine(1)In with treat dry
Material discharged after heat exchange, and the conduction oil after heat exchange cooling returns to heat-conducting oil furnace heat temperature raising again;Without other used heat row
Put;
3), one effect drying machine(1)Discharge:Pass through an effect drying machine(1)Dried dry material passes through an effect drying machine(1)With
Two effect drying machines(2)The pressure difference shielding system 9 of UNICOM is discharged into two effect drying machines(2);Both an effect drying machine had been ensured(1)It is dried
Dry material is discharged, and is ensured simultaneously to an effect drying machine(1)With two effect drying machines(2)Pressure difference isolation is carried out, keeps one to imitate drying
Machine(1)Operation under positive pressure and two effect drying machines(2)Run under negative pressure;
4)One effect drying machine(1)Exhaust emissions, one effect drying machine(1)Tail gas discharge be the dust-laden steam with pressure, lead to
Cross indirect steam and recycle heat source system(4)Come what is completed, two effect drying machines are used as after dust separation(2)Thermal source;
5)Two effect drying machines(2)Charging:One is to add material to be dried by sealed feed system (8), enters back into two effect dryings
Machine(2)In cavity;Two be by an effect drying machine(1)With two effect drying machines(2)The pressure difference shielding system of UNICOM adds two and imitates drying
Machine(2);
6), two effect drying machines(2)The thermal source of heat drying:It is an effect drying machine(1)The tail gas of discharge, an effect drying machine(1)Row
The tail gas gone out recycles heat source system by indirect steam(4)The clean steam with pressure after purification enters two effect dryings
Machine(2), with two effect drying machines(2)In be mutually changed into condensed water after after dry material heat exchange and discharged by draining system;
7), two effect drying machines(2)Discharge:Two effect drying machines(2)It is negative pressure drying, two imitates drying machine in the drying process(2)
Pressure in housing is less than environment atmospheric pressure;Two effect drying machines(2)Dried material is by sealing discharging system (10) discharge;
8), two effect drying machines(2)Exhaust emissions:Two effect drying machines(2)The tail gas of discharge is negative pressure dust-laden steam, two effect dryings
Machine(2)The vent gas treatment of discharge is by drying tail gas vacuum system(7)Complete, set up and maintain by tail gas vacuum system
Two effect drying machines(2)Drying machines are imitated in interior vacuum state, reduction and holding two(2)The volatilization temperature of interior material hygroscopic water;So that
Two effect drying machines(2)Thermal source and treat that dry material keeps larger thermograde, improve two and imitate drying machines(2)Drying efficiency;
B. the thermal source that is used of processing liquid material to be dried is the technique of conduction oil, and its step is as follows:
One effect drying machine(1)With two effect drying machines(2)Thermal source, discharge, exhaust emissions with A. processing cream pasty state, aqueous powder or
The technique of filter cake shape material to be dried;When it is liquid material to handle material to be dried, its step is as follows:
1), one effect drying machine(1)Charging:One effect drying machine(1)For positive pressuring drying, liquid treats that dry material passes through pipe by charge pump
Road and valve are directly added into, and feed pressure and flow are by the valve regulated of sealed feed system, and feeding quantity is by automatic control system
Control;
2), two effect drying machines(2)Charging:Two effect drying machines(2)For negative pressure drying, it is high-order that liquid treats that material is added by charge pump
Pressure stabilizing tank, high-order pressure stabilizing tank keeps stable material position pressure to treat that dry material adds two and imitates drying machine(2), keep two to imitate drying machine
(2)The stabilization of feed pressure and flow;Feeding quantity is by automatic control system control;Add liquid object excessive in high-order pressure stabilizing tank
Material returns to storage tank by overflow pipe;
3), charging carry out state or charging halted state, sealed feed system(12)One is all kept to imitate drying machine(1)Malleation
State is run and two effect drying machines(2)Negative pressure state is run;
So sealed feed system(12)It is made up of charge pump, high-order pressure stabilizing tank, pipeline and valve, and due to an effect drying machine
(1)Positive pressuring drying, two effect drying machines(2)For negative pressure drying, feed pressure is also variant.
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112013670A (en) * | 2020-07-29 | 2020-12-01 | 北京中环弘晟环境科技有限公司 | Energy-saving multi-effect high-moisture material drying device and drying method thereof |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102506573A (en) * | 2011-11-04 | 2012-06-20 | 石家庄工大化工设备有限公司 | Method for indirectly recovering waste gas and waste heat of dryer by compression heat pump |
CN102741638A (en) * | 2009-12-30 | 2012-10-17 | 得利满公司 | Method and facility for drying pasty materials, in particular sludge from wastewater treatment plants and generation of thermal energy |
CN105466157A (en) * | 2015-12-25 | 2016-04-06 | 孙发喜 | Vacuum tube bundle drying system with waste heat for multiple-effect evaporation and pneumatic drying |
CN105466196A (en) * | 2015-12-25 | 2016-04-06 | 孙发喜 | Double-effect vacuum tube bundle drying system |
CN206831934U (en) * | 2017-04-05 | 2018-01-02 | 洛阳瑞岛干燥工程有限公司 | A kind of efficient energy-saving drying system of High water cut material |
-
2017
- 2017-06-14 CN CN201710445868.6A patent/CN107084596A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102741638A (en) * | 2009-12-30 | 2012-10-17 | 得利满公司 | Method and facility for drying pasty materials, in particular sludge from wastewater treatment plants and generation of thermal energy |
CN102506573A (en) * | 2011-11-04 | 2012-06-20 | 石家庄工大化工设备有限公司 | Method for indirectly recovering waste gas and waste heat of dryer by compression heat pump |
CN105466157A (en) * | 2015-12-25 | 2016-04-06 | 孙发喜 | Vacuum tube bundle drying system with waste heat for multiple-effect evaporation and pneumatic drying |
CN105466196A (en) * | 2015-12-25 | 2016-04-06 | 孙发喜 | Double-effect vacuum tube bundle drying system |
CN206831934U (en) * | 2017-04-05 | 2018-01-02 | 洛阳瑞岛干燥工程有限公司 | A kind of efficient energy-saving drying system of High water cut material |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112013670A (en) * | 2020-07-29 | 2020-12-01 | 北京中环弘晟环境科技有限公司 | Energy-saving multi-effect high-moisture material drying device and drying method thereof |
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