CN106766828A - Brown coal drying and upgrading and Water Sproading is dried using technique and its system - Google Patents
Brown coal drying and upgrading and Water Sproading is dried using technique and its system Download PDFInfo
- Publication number
- CN106766828A CN106766828A CN201610996706.7A CN201610996706A CN106766828A CN 106766828 A CN106766828 A CN 106766828A CN 201610996706 A CN201610996706 A CN 201610996706A CN 106766828 A CN106766828 A CN 106766828A
- Authority
- CN
- China
- Prior art keywords
- lignite
- upgrading
- brown coal
- preheater
- heating tube
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 62
- 239000003077 lignite Substances 0.000 title claims abstract description 59
- 238000001035 drying Methods 0.000 title claims abstract description 28
- 238000000034 method Methods 0.000 title claims abstract description 21
- 239000007788 liquid Substances 0.000 claims abstract description 68
- 239000000428 dust Substances 0.000 claims abstract description 6
- 239000003245 coal Substances 0.000 claims abstract description 5
- 238000001704 evaporation Methods 0.000 claims abstract description 3
- 238000000926 separation method Methods 0.000 claims description 38
- 238000010438 heat treatment Methods 0.000 claims description 35
- 239000004744 fabric Substances 0.000 claims description 8
- 238000007599 discharging Methods 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 5
- 238000004062 sedimentation Methods 0.000 claims description 3
- 239000002699 waste material Substances 0.000 abstract 1
- 238000009833 condensation Methods 0.000 description 7
- 230000005494 condensation Effects 0.000 description 7
- 238000011084 recovery Methods 0.000 description 4
- 239000002245 particle Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 230000003020 moisturizing effect Effects 0.000 description 1
- 230000006855 networking Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Classifications
-
- 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
- F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
- F26B17/12—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft
- F26B17/16—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft the materials passing down a heated surface, e.g. fluid-heated closed ducts or other heating elements in contact with the moving stack of material
-
- 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
- F26B25/005—Treatment of dryer exhaust gases
-
- 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
- F26B25/06—Chambers, containers, or receptacles
- F26B25/08—Parts thereof
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B3/00—Drying solid materials or objects by processes involving the application of heat
- F26B3/18—Drying solid materials or objects by processes involving the application of heat by conduction, i.e. the heat is conveyed from the heat source, e.g. gas flame, to the materials or objects to be dried by direct contact
- F26B3/22—Drying solid materials or objects by processes involving the application of heat by conduction, i.e. the heat is conveyed from the heat source, e.g. gas flame, to the materials or objects to be dried by direct contact the heat source and the materials or objects to be dried being in relative motion, e.g. of vibration
- F26B3/26—Drying solid materials or objects by processes involving the application of heat by conduction, i.e. the heat is conveyed from the heat source, e.g. gas flame, to the materials or objects to be dried by direct contact the heat source and the materials or objects to be dried being in relative motion, e.g. of vibration the movement being performed by gravity
-
- 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
Abstract
The present invention relates to a kind of brown coal drying and upgrading and dry Water Sproading and utilize technique, solve the problems, such as steam heat energy and water resource waste that existing brown coal drying and upgrading evaporates.Method includes the steam for obtaining moisture-free coal and evaporating after being dried in lignite feeding drier, the lignite first to be sent into be re-fed into after preheating in preheater and dry in drier, it is then exhausted from after lignite indirect heat exchange in feeding preheater after the steam removing dust device dedusting drawn in the drier, the condensate liquid of generation sends into water treatment system treatment after collecting.Present invention process is simple, can effectively reclaim dry steam heat energy and water resource, equipment investment and operating cost are low, safe and reliable.
Description
Technical field
The present invention relates to a kind of brown coal drying technique and system, specifically a kind of brown coal drying and upgrading and dry water return
Receive and utilize technique and its system.
Background technology
In traditional brown coal drying and upgrading technique, the lignite of high-moisture is sent directly into drier and is dried, therebetween
A large amount of more than 100 DEG C steam can be produced, these steam are difficult to back because temperature is high, complicated, the problems such as reclaim high energy consumption
Receive and utilize, can only directly be vented, lost the water resource of preciousness, while heat (including the latent heat carried in also lost steam
And sensible heat), for some regional lignite, drying containing a small amount of pollutant (COD is higher) in water, directly emptying is also resulted in
Water pollution and atmosphere pollution.Such as the method for the brown coal drying and upgrading of application number 201210583274.9, disclose carries out two by lignite
Secondary drying, but it is not related to the processing method of dry steam.Synchronization for the heat energy and water of this part steam so far is returned
Receive also without preferable method.
The content of the invention
The invention aims to solve above-mentioned technical problem, there is provided a kind of process is simple, can effectively reclaim dry steaming
Low, the safe and reliable brown coal drying and upgrading of the heat energy and water resource of vapour, equipment investment and operating cost and dry Water Sproading utilization
Technique.
The present invention also provides that a kind of system for above-mentioned technique is extremely simple, is easy to transformation, the coal that security reliability is good
Drying and upgrading and dry Water Sproading and utilize system.
Technical scheme includes the steam for obtaining moisture-free coal and evaporating after being dried in lignite feeding drier, the lignite
It is re-fed into being dried in drier after first being preheated in feeding preheater, is sent into after the steam removing dust device dedusting that the drier is drawn
It is then exhausted from after lignite indirect heat exchange in preheater, the condensate liquid of generation sends into water treatment system treatment after collecting.
The lower housing section of the preheater is provided with lower heating tube bundle, and epimere is provided with heating tube bundle, and the steam is first sent into
With lignite indirect heat exchange in the lower heating tube bundle of preheater, then after isolating condensate liquid through gas-liquid separation chamberHeated in inflow
It is vented after tube bank and the further indirect heat exchange of lignite；Gas-liquid separation chamberThe condensate liquid feeding water treatment system treatment isolated.
Into the lignite 30~50wt% of water content before preheater, the lignite water content for going out preheater declines a 10wt% left sides
It is right.
The stage casing of the device preheater is provided with baffle plate, and the steam produced in lignite warm rises to condensation shape at baffle plate
Into condensed water, the condensed water flows into dirt liquid collection separation chamber along baffle plate carries out dirt liquid carries out sedimentation separation, and dirt liquid is collected and separated
Discharge mud, top overflow clarified solution, the clarified solution feeding water treatment system treatment in room bottom.
Present system includes drier and preheater, and the preheater includes housing, and the case top sets charging aperture,
Bottom sets out material mouth, and top sets air-vent, bottom and sets air inlet, and epimere is provided with the upper heating tube of lateral arrangement in the housing
Beam, hypomere is provided with the lower heating tube bundle of lateral arrangement, and the air inlet is through lower heating tube bundle, gas-liquid separation chamber, upper heating tube bundle
Connected with air-vent；The charging aperture of the drier is connected with the discharging opening of preheater, and the moisture outlet of the drier is through removing
Dirt device is connected with the air inlet of drier, and the condensation-water drain of the gas-liquid separation chamber is connected with water treatment system.
Stage casing also sets the multi-row staggered baffle plate being evenly arranged in the housing, and one end of the baffle plate is collected with dirt liquid and separated
Room connects, and baffle plate collects separation chamber direction and has downward level inclination along dirt liquid, and the dirt liquid collects the clarification of separation chamber
Liquid outlet is connected with water treatment system.
The section of the plate washer is inverted V-shaped, and the angle of its inverted V-shaped is 60~140 °.
The level inclination of the baffle plate is 0.36~1.62 °.
Steam cloth air chamber is provided with the air inlet；Fixed gas collecting chamber is provided with the air-vent.
The upper and lower heating tube bundle is downward-sloping along gas flow direction, and its level inclination is 0.36~1.62 °.
For problem present in background technology, inventor has connected a preheater before drier, is entering lignite
To enter first preheated in preheater before drying machine, and the heat energy then steam from drying machine, will the steam drawn of drying machine introduce
Indirectly heat is carried out in preheater to lignite, on the one hand recyclable heat energy, on the other hand reclaims the condensate liquid that moisture condensation is obtained,
The condensate liquid of recovery can play the purpose of saving water resource after treatment as plant circulation cold water moisturizing.Meanwhile, inventor couple
Preheater has been also carried out improving, and changes route of the aqueous vapor in preheater, at utmost reclaims condensate liquid, improves equipment
Service life, reduce block the problems such as occur, it is specific as follows：(1) upper and lower heating tube bundle is set, steam is introduced into heating tube
Indirect preheating is carried out to the lignite fallen in housing in beam, the condensate liquid produced in lower heating tube bundle warm is in gas-liquid separation
Interior is separated and collected, and the condensate liquid of the generation in upper heating tube bundle warm is separated and collected in fixed gas collecting chamber, is realized
The recovery of the heat energy and water resource of steam, separates the steam after condensate liquid and goes successively to heating tube bundle and further changed with lignite
Heat；(2) baffle plate is set between upper and lower heating tube bundle, and the baffle plate that the steam that lignite is volatilized rises to multi-layer intercrossed arrangement enters
And condense, condensate liquid collects inflow dirt liquid and collects separation chamber along this baffle plate, pre-dried condensate liquid is recycled profit
With, water source money is further reclaimed, mitigate environmental pollution.(3) gas-liquid separation chamber and dirt liquid collect the condensate liquid collected in separation chamber
Can send into after water treatment system treatment is further processed and reclaim, synchronously realize drying the condensation in steam using a preheater
The recovery of the condensate liquid in liquid and lignite warm, achieves many things at one stroke, with significant technique effect.
The baffle plate is preferably inverted " v ", multi-layer intercrossed arrangement, it is ensured that lignite particle can be passed through without blocking up
Material.All baffle plates have downward inclination angle (preferably 0.36~1.62 °) along separation chamber directions are collected, it is ensured that the drop of condensation can be with
Smoothly collect and flow into collection chamber receiving condensate.The scope of v-angle can be at 60~140 °, it is ensured that will not be because of the obstruction of two flanks
Material is caused to flow down difficulty.
Enter gas-liquid separation to ensure in bottom moisture condensation room and top exhaust gas chamber that steam condensate smoothly collects cocurrent
Room and on-condensible gas collecting chamber, the upper and lower heating tube bundle are downward-sloping along gas flow direction, and its level inclination is 0.36
~1.62 °.
Beneficial effect：
(1) present invention reduces factory's thermic load using the energy preheating lignite entrained by the steam escaped in drier
(more than 45%), it is energy-saving；
(2) moisture escaped in drier is reclaimed, the water resource of preciousness in lignite is fully recycled, lignite can be reclaimed
More than the 43% of middle moisture；
(3) steam that lignite in preheater is volatilized can be reclaimed, it is to avoid lignite is on the top of preheater because on absorbing
Rise steam and build bridge, cause lignite particle smoothly to flow down discharge, the condensate liquid of all recovery is reclaimed after treatment, to ring
Border is friendly；
(4) present system is simple, technique is easy, and equipment investment and operating cost are low, safe and reliable.
Brief description of the drawings
Fig. 1 is present invention process flow chart and system diagram.
Fig. 2 is preheater structure chart.Fig. 3 is the A-A sectional views of Fig. 1.
Wherein, 1- housings, 2- charging apertures, 3- discharging openings, 4- gas-liquid separation chamber, 5- fixed gas collecting chambers, 6- dirt liquid is collected
Separation chamber, heating tube bundle, 10- air-vents, 11- air inlets, 12- baffle plates, 13- under 7- steam cloth air chamber, the upper heating tube bundles of 8-, 9-
Drier, 14- dedusters, 15- water treatment systems, 16- preheaters.
Specific embodiment
Explanation is further explained to present system below in conjunction with the accompanying drawings：
Referring to Fig. 1, the series connection drier 13 of preheater 16, the drier 13 can be 1 or many connection in series-parallel, the drying
The charging aperture of device 13 is connected with the discharging opening of preheater 16, moisture outlet removing dust device 14 and the drier 13 of the drier 13
Air inlet is connected.
The preheater 16 includes housing 1, and the top of the housing 1 sets charging aperture 2, and bottom sets out material mouth 3, and top sets air inducing
Mouth 10, bottom sets air inlet 11, and steam cloth air chamber 7 is provided with the air inlet 11；Fixed gas receipts are provided with the air-vent 10
Collection room 5.Epimere is provided with the upper heating tube bundle 8 of lateral arrangement in the housing 1, and hypomere is provided with the lower heating tube bundle 9 of lateral arrangement,
The steam cloth air chamber 7 is connected through lower heating tube bundle 9, gas-liquid separation chamber 4, upper heating tube bundle 8 with fixed gas collecting chamber 5, described
Upper and lower heating tube bundle 8,9 is downward-sloping along gas flow direction, and its level inclination c is 0.36~1.62 °.The housing 1
Interior stage casing also sets the multi-row staggered baffle plate 12 being evenly arranged, and one end and the dirt liquid of the baffle plate 12 are collected separation chamber 6 and is connected, and gear
Plate 12 collects the direction of separation chamber 6 along dirt liquid has a downward level inclination, the level inclination a of the baffle plate 12 for 0.36~
1.62 °, the section of the plate washer 12 is inverted V-shaped, and angle b is 60~140 °.
The gas-liquid separation chamber 4, the solidifying gas collecting chamber 5, condensate outlet of steam cloth air chamber 7 and cold dirt liquid are collected and separated
The clarified solution outlet of room 6 is connected with water treatment system 15.
Operation principle：
Raw material lignite (water content 30wt%) is continuously added in preheater 16 from charging aperture 1, is flowed downward first through upper heating
Tube bank 7 is exchanged heat with the steam in pipe, is then uniformly distributed through multi-layer intercrossed arrangement baffle plate 12, then through lower heating tube bundle 8 and
Steam in pipe further exchanges heat, and lignite temperature can reach 46 DEG C when reaching discharging opening 2, and water content can be down to 20wt%,
The final bottom discharge from preheater 16 mouthful 8 is continuously discharged into drier 13 and is further dried to below water content 7wt%.It is dry
The steam that drying is evaporated in dry device 13 removes the fine dust particles wherein carried secretly through moisture outlet feeding deduster 14, so
The air inlet 11 of preheater 16 is re-fed into afterwards.
In preheater 16, the steam produced in lignite warm is risen at the baffle plate 12 of uniform interlaced arrangement, quilt
Stop and formed the lower surface that condensate liquid is attached to baffle plate 12, the dust-laden condensate liquid that baffle plate 12 is collected flows into dirt liquid and collects separation chamber
6, dirt liquid separation is further carried out in dirt liquid collects separation chamber 6, collect condensate liquid；On the other hand, drawn in drier 13
Steam (105 DEG C, 0.1MPa) enters lower heating tube bundle 9 after entering steam cloth air chamber 7 uniformly by air inlet 11 by the hypomere of housing 1
Lignite heat exchange with housing 1, undergoes phase transition condensation herein, discharges heat lignite, is separated subsequently into gas-liquid separation chamber 4
Condensate liquid in steam, fixed gas is further brown to preheating by the upper heating tube bundle 8 that gas-liquid separation chamber 4 enters back into the epimere of housing 1
Coal, condensed water is further separated out subsequently into fixed gas collecting chamber 5, and fixed gas is in the presence of air-introduced machine by the row of air-vent 10
Go out, now gas temperature is (40 DEG C).
Condensate liquid in the gas-liquid separation chamber 4 and fixed gas collecting chamber 5 and steam cloth air chamber 7 can be by condensation-water drain
Discharge, dirt liquid collect separation chamber 6 in collect dust-laden condensate liquid after sedimentation separation, bottom discharge mud, top overflow it is clear
The clarified liquid outlet discharge of clear liquid, the condensate liquid of discharge sends into reuse after water treatment system 6 is processed.The water treatment system
6 can use biological oxidation system or other existing water treatment systems suitable for industry condensation water process, this area skill
Art personnel can rationally select suitable as needed, to meet recycle-water (being such as incorporated to circulating water networking) standard.
Claims (10)
1. a kind of brown coal drying and upgrading and dry Water Sproading and utilize technique, including will lignite send into dry in drier after done
Dry coal and the steam for evaporating, it is characterised in that the lignite first to be sent into be re-fed into after preheating in preheater and dry in drier,
It is then exhausted from after lignite indirect heat exchange in feeding preheater after the steam removing dust device dedusting drawn in the drier, generation
Condensate liquid sends into water treatment system treatment after collecting.
2. brown coal drying and upgrading as claimed in claim 1 and dry Water Sproading and utilize technique, it is characterised in that the preheater
Lower housing section be provided with lower heating tube bundle, epimere is provided with heating tube bundle, and the steam first sends into the lower heating tube bundle of preheater
In with lignite indirect heat exchange, then upper heating tube bundle flowed into after isolating condensate liquid through gas-liquid separation chamber further changed indirectly with lignite
It is vented after heat；Gas-liquid separation chamber goes out the condensate liquid feeding water treatment system treatment isolated.
3. brown coal drying and upgrading as claimed in claim 1 or 2 and dry Water Sproading and utilize technique, it is characterised in that enter pre-
Lignite 30~50wt% of water content before hot device, the lignite water content for going out preheater declines 10wt% or so.
4. brown coal drying and upgrading as claimed in claim 1 or 2 and dry Water Sproading and utilize technique, it is characterised in that be described pre-
The stage casing of hot device is provided with baffle plate, and the steam produced in lignite warm rises to and condensed at baffle plate to form condensed water, described cold
Solidifying water flows into dirt liquid collection separation chamber along baffle plate carries out dirt liquid carries out sedimentation separation, and dirt liquid collects separation chamber bottom discharge mud,
Top overflow clarified solution, the clarified solution feeding water treatment system treatment.
5. a kind of brown coal drying and upgrading and dry Water Sproading and utilize system, including drier, it is characterised in that also include preheating
Device, the preheater includes housing, and the case top sets charging aperture, and bottom sets out material mouth, top set air-vent, bottom set into
Gas port, epimere is provided with the upper heating tube bundle of lateral arrangement in the housing, and hypomere is provided with the lower heating tube bundle of lateral arrangement, described
Air inlet is connected through lower heating tube bundle, gas-liquid separation chamber, upper heating tube bundle with air-vent；The charging aperture of the drier and preheating
The discharging opening connection of device, the moisture outlet removing dust device of the drier is connected with the air inlet of preheater, the gas-liquid separation
The condensation-water drain of room is connected with water treatment system.
6. brown coal drying and upgrading as claimed in claim 5 and dry Water Sproading and utilize system, it is characterised in that in the housing
Stage casing also sets the multi-row staggered baffle plate being evenly arranged, and one end and the dirt liquid of the baffle plate are collected separation chamber and is connected, and baffle plate is along dirt
Liquid collects separation chamber direction has downward level inclination, and the dirt liquid collects clarified solution outlet and the water treatment system of separation chamber
Connection.
7. brown coal drying and upgrading as claimed in claim 6 and dry Water Sproading and utilize system, it is characterised in that the plate washer
Section is inverted V-shaped, and the angle of its inverted V-shaped is 60~140 °.
8. brown coal drying and upgrading as claimed in claim 6 and dry Water Sproading and utilize system, it is characterised in that the baffle plate
Level inclination is 0.36~1.62 °.
9. brown coal drying and upgrading as described in claim any one of 5-8 and dry Water Sproading and utilize system, it is characterised in that institute
State and be provided with air inlet steam cloth air chamber；Fixed gas collecting chamber is provided with the air-vent.
10. brown coal drying and upgrading as claimed in claim 6 and dry Water Sproading and utilize system, it is characterised in that be described upper and lower
Heating tube bundle is downward-sloping along gas flow direction, and its level inclination is 0.36~1.62 °.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610996706.7A CN106766828A (en) | 2016-11-11 | 2016-11-11 | Brown coal drying and upgrading and Water Sproading is dried using technique and its system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610996706.7A CN106766828A (en) | 2016-11-11 | 2016-11-11 | Brown coal drying and upgrading and Water Sproading is dried using technique and its system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106766828A true CN106766828A (en) | 2017-05-31 |
Family
ID=58973447
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610996706.7A Pending CN106766828A (en) | 2016-11-11 | 2016-11-11 | Brown coal drying and upgrading and Water Sproading is dried using technique and its system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106766828A (en) |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AU5573780A (en) * | 1979-02-12 | 1980-08-21 | John Michael Chambers | Drying process and apparatus |
| RU2222752C2 (en) * | 2001-12-24 | 2004-01-27 | Евсеев Геннадий Александрович | Water-heating plant for heating purposes and/or hot-water supply, cooled condensate return tank of plant, and liquid-to-liquid heat exchanger of plant |
| CN201569251U (en) * | 2009-12-25 | 2010-09-01 | 山东天力干燥设备有限公司 | Oxygen-free lignite drying system |
| CN201569260U (en) * | 2009-12-28 | 2010-09-01 | 山东天力干燥设备有限公司 | Indirect heat-exchange rotation superheating steam brown coal drying system |
| EP2495495A2 (en) * | 2011-03-02 | 2012-09-05 | Babcock Borsig Steinmüller GmbH | Fluidised bed drier system |
| CN102967121A (en) * | 2012-11-30 | 2013-03-13 | 山东科院天力节能工程有限公司 | Lignite drying system and technology with superheated steam capable of recycling waste steam heat |
| CN205175027U (en) * | 2015-11-23 | 2016-04-20 | 四川农业大学 | Can collect liquid hot air drying equipment |
| CN206176948U (en) * | 2016-11-11 | 2017-05-17 | 中国五环工程有限公司 | Matter and dry water recycle system are put forward to brown coal drying |
-
2016
- 2016-11-11 CN CN201610996706.7A patent/CN106766828A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AU5573780A (en) * | 1979-02-12 | 1980-08-21 | John Michael Chambers | Drying process and apparatus |
| RU2222752C2 (en) * | 2001-12-24 | 2004-01-27 | Евсеев Геннадий Александрович | Water-heating plant for heating purposes and/or hot-water supply, cooled condensate return tank of plant, and liquid-to-liquid heat exchanger of plant |
| CN201569251U (en) * | 2009-12-25 | 2010-09-01 | 山东天力干燥设备有限公司 | Oxygen-free lignite drying system |
| CN201569260U (en) * | 2009-12-28 | 2010-09-01 | 山东天力干燥设备有限公司 | Indirect heat-exchange rotation superheating steam brown coal drying system |
| EP2495495A2 (en) * | 2011-03-02 | 2012-09-05 | Babcock Borsig Steinmüller GmbH | Fluidised bed drier system |
| CN102967121A (en) * | 2012-11-30 | 2013-03-13 | 山东科院天力节能工程有限公司 | Lignite drying system and technology with superheated steam capable of recycling waste steam heat |
| CN205175027U (en) * | 2015-11-23 | 2016-04-20 | 四川农业大学 | Can collect liquid hot air drying equipment |
| CN206176948U (en) * | 2016-11-11 | 2017-05-17 | 中国五环工程有限公司 | Matter and dry water recycle system are put forward to brown coal drying |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102992575B (en) | Steam thermal cycle sludge drying method and system | |
| CN110207484B (en) | Material drying evaporation gas recycling system and method | |
| CN107285592A (en) | A kind of double-stage tandem type heat pump sludge drier | |
| CN101830624B (en) | System and process for drying sludge blades | |
| CN103601355A (en) | Spiral sludge drier | |
| CN1533991A (en) | Power generating heat supplying clean production system using city sewage and garbage resources | |
| CN109432808A (en) | Energy-saving and environment-friendly DDGS waste heat vapo(u)rization system | |
| CN107648874A (en) | A kind of volatile solvent condensate recycling device | |
| CN110182874A (en) | A kind of super low energy consumption flash concentration desulfurization wastewater and industrial brine waste zero emission system | |
| CN202358984U (en) | Ash sluicing water treatment and cyclic utilization system for dry pulverized coal gasification device | |
| CN203048755U (en) | Steam heat-cycling sludge drying system | |
| CN206176948U (en) | Matter and dry water recycle system are put forward to brown coal drying | |
| CN211284125U (en) | Multi-effect short-distance heat transfer drying system | |
| CN104724776B (en) | Devices and methods therefor in pressure evaporating indirect steam incorporation press water | |
| CN208776558U (en) | Sludge drying and tail gas recycle concentration device | |
| CN211284122U (en) | Superheated steam sludge drying system | |
| CN107245343A (en) | A kind of coke wet quenching high temperature steam treatment method | |
| CN107162102A (en) | A kind of dehydrating and drying method of gasification system fine slag slurries and its dehydration drying system used | |
| CN208586191U (en) | A kind of sludge drying mechanism based on waste heat integration | |
| CN106766828A (en) | Brown coal drying and upgrading and Water Sproading is dried using technique and its system | |
| CN208166828U (en) | A kind of sludge drying system | |
| CN216347662U (en) | Material drying device with high circulating heat efficiency | |
| CN206176941U (en) | Matter is put forward with equipment of preheating to brown coal drying | |
| CN107090302A (en) | A kind of coke wet quenching high temperature steam treatment device | |
| CN110772938B (en) | Intensive smoke plume treatment and purification system and method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170531 |
|
| RJ01 | Rejection of invention patent application after publication |