CN107227189A - The steam-cured processing system of lignite - Google Patents
The steam-cured processing system of lignite Download PDFInfo
- Publication number
- CN107227189A CN107227189A CN201710558481.1A CN201710558481A CN107227189A CN 107227189 A CN107227189 A CN 107227189A CN 201710558481 A CN201710558481 A CN 201710558481A CN 107227189 A CN107227189 A CN 107227189A
- Authority
- CN
- China
- Prior art keywords
- steam
- cured
- kettle
- pipe
- processing system
- 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
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/04—Raw material of mineral origin to be used; Pretreatment thereof
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L9/00—Treating solid fuels to improve their combustion
- C10L9/08—Treating solid fuels to improve their combustion by heat treatments, e.g. calcining
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/08—Drying or removing water
Abstract
The invention discloses a kind of steam-cured processing system of lignite, belong to pressure vessel；Aim to provide a kind of high, easy to operate capacity utilization, service life length, the steam-cured processing unit for saving the energy.It includes two steam-cured kettles；Steam-cured kettle is made up of the kettle body body (2) with top cover (1) and bottom (11), the epimere steam pipe (5) in kettle body body (2), hypomere steam pipe (6) and pumping drain pipe (3)；Each epimere steam pipe (5) one end in two steam-cured kettles is connected with the first distribution cylinder (17) connection, the other end by the way that external pipe is corresponding, each hypomere steam pipe (6) one end in two steam-cured kettles is connected with the second distribution cylinder (15) connection, the other end by the way that external pipe is corresponding, and each pumping drain pipe (3) in two steam-cured kettles connects with moisture separator (18)；Two passages (9) are connected with nitrogen gas generating device (10).Simple in construction, efficiency high of the invention；It is a kind of steam curing device for handling particulate species material.
Description
Technical field
The present invention relates to a kind of steam-cured processing unit, more particularly to a kind of steam curing device handled for lignite upgrading；Category
In pressure vessel.
Background technology
Steam-cured kettle is also known as still kettle, is a kind of large pressurized vessel, is commonly horizontal type structure；Built available for air entrained concrete
Block, concrete tubular pile, Dinas brickes, coal-dust brick, calcium silicate board with microporous, New Type Light-weight Wall Material, insulation asbestos board, high intensity stone
The construction materials such as cream carry out steam press maintenance, and purposes is quite varied.
Lignite water content and oxygen content are high, calorific value is low, easy spontaneous combustion and weathering, store more difficult；In order to effectively using brown
Coal, it usually needs it is dried upgrading processing.However, (adsorbing water in water in lignite and being stored in lignite texture and capillary
Capillary water in pipe) handled through drying and upgrading and after being removed, inside lignite and surface can leave substantial amounts of crack and texture, more
Easy oxidation by air heating and spontaneous combustion；Need to fill lignite crack and texture using nitrogen, to suppress its oxidation.
At present, upgrading processing lignite generally is dried using horizontal steam-cured kettle；Bothered in the presence of charging and draw operation,
Efficiency is low, floor space is big, capacity utilization is low, be not provided with nitrogen supplementary device, the easy corrosion and damage of kettle body body, waste heat
The defect such as utilization rate is low, energy consumption is high.Concrete analysis is as follows：
1) lignite be particulate species loose unpacked material, therefore typically will by container load could be fed, draw operation；
Time-consuming, efficiency is low.
2) loaded using container and be difficult to fill up in space in kettle, capacity utilization is low.
3) without nitrogen supplementary device, it is impossible to inject nitrogen filling lignite crack and texture into kettle.
4) the easy corrosion and damage because of electrochemical reaction of kettle body body：In order to avoid boiler corrosion and fouling is avoided, stove
Water is usually pH10 or so.When being passed through in weakly alkaline steam (equivalent to electrolyte) in kettle, between kettle body body and lignite
Be easy to turn on and form two electrodes (equivalent to large-scale galvanic cell)；In addition the factor such as temperature in the kettle, pressure is present, and accelerates original
Cell oxidation reduction reaction, so as to cause, to kettle body body fast erosion, to directly affect steam-cured kettle service life.
5) generally all it is directly to discharge the high-temperature steam in kettle when needing release to cool after the completion of steam-cured operation, it is remaining
Heat utilization is insufficient.
The content of the invention
For drawbacks described above present in prior art, the present invention is intended to provide a kind of capacity utilization is high, input and output material behaviour
Make convenience, service life length, save the energy, the steam-cured processing system of lignite of lignite spontaneous combustion can be avoided.
To achieve these goals, the present invention uses following technical scheme：It includes steam-cured kettle；The steam-cured kettle is two
It is individual, each steam-cured kettle by can-like structure and vertically fixed kettle body body, be fixed on the kettle body body upper port top cover, with should
Passage that kettle body body lower port is docked and connected and is in tilted layout, it is fixed on the bottom of the passage port of export, positioned at kettle body
In body and by the equally distributed many epimere steam pipes of vertical mode and Duo Gen hypomeres steam pipe and many pumping drain pipes
Constitute；One end of each epimere steam pipe in two steam-cured kettles respectively with first distribution cylinder connect, the other end respectively by with
The external pipe correspondence of valve is connected, one end of each hypomere steam pipe in two steam-cured kettles connects with the second distribution cylinder respectively,
The other end is connected by the other valvular external pipe correspondence of band respectively, each pumping drain pipe one end in two steam-cured kettles point
Do not connected with moisture separator；Two passages are connected with nitrogen gas generating device respectively.
The moisture separator by be connected with pumping drain pipe moisture separator, by the moisture separator and soft water pond
The water pump of connection is constituted；Have discharger in passage, the discharger by be horizontally arranged in passage two rotating shafts, be fixed on
Polylith blade in each rotating shaft is constituted；The lower semisection of kettle body body has and its internal air bubble connector connected；In nitrogen hair
The first magnetic valve and blowoff valve are mounted on connecting pipeline between generating apparatus and each passage, in the first distribution cylinder and respectively
It is mounted on the connecting pipeline of epimere steam pipe and on connecting pipeline of the second distribution cylinder with each hypomere steam pipe another
The first outer magnetic valve；Multiple sensors are distributed with kettle body body；Have vertically fixed electrode in kettle body body, each electrode with
The positive pole electrical connection of dc source, the inwall of each kettle body body is electrically connected with the negative pole of the dc source.
Compared with the prior art, the present invention by adopting the above-described technical solution, there is an advantage in that：
1) kettle body body uses vertical arrangement, can be by granular lignite in bulk from upper by belt conveyor
Port is sent directly into kettle, and thoroughly avoiding horizontal steam-cured kettle needs first to load the trouble that could send into lignite in kettle with container；
Not only improve powder feeding efficiency but also can have been filled up in space in kettle automatically using lignite free-falling, and improve the volume of steam-cured kettle
Utilization rate.
2) due to being provided with openable bottom in the lower port of kettle body body, thus it is straight using the own wt of lignite
Run in material, not only convenient and swift but also improve discharging efficiency.
3) due to adding electrode in kettle body body, therefore it can be avoided because of electrochemical reaction using accessory power supply
The defect for causing kettle body body to be corroded and damaged, extends service life.
4) due to adding the nitrogen gas generating device connected with kettle, therefore can be by vacuum after drying and upgrading is finished
Pump will be vacuumized in kettle, and inject nitrogen filling lignite crack and texture；Thoroughly prevented lignite dieseling, it is ensured that storage and
Transport safely at a distance.
5) adjacent two-stage steam-cured kettle is connected as a result of external pipe, arrived when the upper level steam-cured kettle heat-insulation pressure keeping time
Remaining pressure and heat can be oriented to by next stage steam-cured kettle by external pipe after up to sets requirement and realize UTILIZATION OF VESIDUAL HEAT IN；Together
When, air water then can be guided to moisture separator by being evacuated drain pipe and reclaim hot water by the residual compression of upper level steam-cured kettle, and
Boiler is returned to recycle.Therefore UTILIZATION OF VESIDUAL HEAT IN is abundant, save the energy.
Brief description of the drawings
Fig. 1 is the structural representation of the present invention；
Fig. 2 is the structural representation of utility model moisture separator；
Fig. 3 is A-A sectional views in Fig. 1.
In figure：Top cover 1, kettle body body 2, pumping drain pipe 3, electrode 4, epimere steam pipe 5, hypomere steam pipe 6, discharger
7th, rotating shaft 7-1, blade 7-2, blowoff valve 8, passage 9, nitrogen gas generating device 10, bottom 11, magnetic valve 12, air bubble connector
13rd, the distribution of dc source 14, second cylinder 15, the distribution of sensor 16, first cylinder 17, moisture separator 18, aqueous vapor separation
Device 18-1, water pump 18-2, soft water pond 18-3.
Embodiment
The invention will be further described with specific embodiment below in conjunction with the accompanying drawings.
As shown in Figures 1 to 3：Two steam-cured kettles are vertically arranged, and each steam-cured kettle is by kettle body fixed in can-like structure and vertically
Body 2, the top cover 1 for being fixed on the kettle body body upper port, leading of being docked and connected and be in tilted layout with the lower port of kettle body body 2
Expects pipe 9, the bottom 11 for being fixed on the passage port of export, in the kettle body body 2 and equally distributed many by vertical mode
Epimere steam pipe 5 and Duo Gen hypomeres steam pipe 6 and many pumping drain pipes 3 constitute, epimere steam pipe 5, hypomere steam pipe 6 with
And it is distributed with some through holes on pumping drain pipe 3.The upper end of each epimere steam pipe 5 in two steam-cured kettles is respectively with external
One distribution cylinder 17 connects, in two steam-cured kettles each epimere steam pipe 5 lower end respectively by with valvular external pipe (in figure
It is not shown) correspondingly connect, the upper end of each hypomere steam pipe 6 in two steam-cured kettles connects with the second external distribution cylinder 15 respectively
The lower end of each hypomere steam pipe 6 passes through the other valvular external pipe (not shown) of band respectively in logical, two steam-cured kettles
The upper end of each pumping drain pipe 3 is connected with moisture separator 18 respectively in correspondence connection, two steam-cured kettles, plug is used in lower end respectively
Closing.Two passages 9 are connected with nitrogen gas generating device 10 respectively, and the purpose is to replaced by injecting high pressure nitrogen in material hole
Residual moisture.
Moisture separator 18 by with pumping drain pipe 3 be connected moisture separator 18-1, by the moisture separator with it is soft
The water pump 18-2 of pond 18-3 connections is constituted.
For the ease of releasing material, it is to avoid material jam；There is discharger 7 in passage 9, the discharger is by being horizontally arranged at
Two rotating shaft 7-1 in passage 9, the polylith blade 7-2 being fixed on each rotating shaft 7-1 are constituted.Blade is driven by rotating shaft 7-1
7-2, which is rotated, can make material loosen and smoothly flow out.
Blocked during in order to avoid discharges material, the lower semisection of kettle body body 2 has and its internal air battery connected
Interface 13；It can loosen material using air bubble and smoothly flow out.
For the ease of controlling on the injection rate of nitrogen, the connecting pipeline between nitrogen gas generating device 10 and each passage 9
It is mounted on the first magnetic valve 12；For the ease of discharge condensed water, the connection between nitrogen gas generating device 10 and each passage 9
Blowoff valve 8 is mounted on pipeline.
For the ease of controlling the injection rate of steam, on connecting pipeline of the first distribution cylinder 17 with each epimere steam pipe 5,
And it is mounted on the first other magnetic valve 12 on connecting pipeline of the second distribution cylinder 15 with each hypomere steam pipe 6.
For the ease of the temperature and pressure in control kettle, multiple sensors 16 are disposed with kettle body body 2.
For the ease of maintenance, the manhole (not indicated in figure) connected with kettle is provided with kettle body body 2.
In order to avoid kettle body body 2 has by support (in figure not because of electrochemical reaction in corrosion and damage, kettle body body 2
Indicate) fixed electrode 4 vertically；Each electrode 4 is electrically connected with the positive pole of external dc source 14, the inwall of each kettle body body 2
Electrically connected with the negative pole of the dc source.
In use, as needed, separately or concurrently distributing one thereto, cylinder 15 by the first distribution cylinder 17, second
Steam-cured kettle (such as that steam-cured kettle of left side) is passed through steam；After the completion of steam-cured, close steam-cured kettle connection first and distribute cylinder 17, the
Two distribution cylinders 15 magnetic valve 12, open another steam-cured kettle (such as that steam-cured kettle of right side) connection first distribute cylinder 17,
The magnetic valve 12 of second distribution cylinder 15, you can by the external pipe by the residual steam and pressure in that steam-cured kettle of left side
Power is oriented in that steam-cured kettle of feeding right side, realizes UTILIZATION OF VESIDUAL HEAT IN.Unlatching is located in that steam-cured kettle of left side on pumping drain pipe 3
Magnetic valve 12, you can by the steam-cured kettle residual steam be pumped into moisture separator 18 carry out aqueous vapor separation, realize hot water
Recycle.
Claims (8)
1. a kind of steam-cured processing system of lignite, including steam-cured kettle；It is characterized in that：The steam-cured kettle be two, each steam-cured kettle by
In can-like structure and vertically fixed kettle body body (2), be fixed on the kettle body body upper port top cover (1), with the kettle body sheet
Passage (9) that body (2) lower port is docked and connected and is in tilted layout, it is fixed on the bottom (11) of the passage port of export, is located at
Kettle body body (2) is interior and presses the equally distributed many epimere steam pipes (5) of vertical mode and many hypomere steam pipes (6) and many
Root pumping drain pipe (3) is constituted；One end of each epimere steam pipe (5) in two steam-cured kettles connects with the first distribution cylinder (17) respectively
The logical, other end with valvular external pipe correspondence respectively by connecting, one end of each hypomere steam pipe (6) in two steam-cured kettles
Connected respectively by the way that other band valvular external pipe is corresponding with the second distribution cylinder (15) connection, the other end respectively, two
Each pumping drain pipe (3) one end in steam-cured kettle is connected with moisture separator (18) respectively；Two passages (9) respectively with nitrogen
Generating means (10) is connected.
2. the steam-cured processing system of lignite according to claim 1, it is characterised in that：Moisture separator (18) by with pumping
The moisture separator (18-1) of drain pipe (3) connection, the water pump (18-2) for connecting the moisture separator with soft water pond (18-3)
Constitute.
3. the steam-cured processing system of lignite according to claim 2, it is characterised in that：There is discharger (7) in passage (9),
The discharger is by two rotating shafts (7-1) being horizontally arranged in passage (9), the polylith blade being fixed in each rotating shaft (7-1)
(7-2) is constituted；The lower semisection of kettle body body (2) has and its internal air bubble connector (13) connected.
4. the steam-cured processing system of lignite according to claim 1 or 2 or 3, it is characterised in that：In nitrogen gas generating device (10)
The first magnetic valve (12) and blowoff valve (8) are mounted on connecting pipeline between each passage (9), cylinder is distributed first
(17) with distributing cylinder (15) and the company of each hypomere steam pipe (6) on the connecting pipeline of each epimere steam pipe (5) and second
Other the first magnetic valve (12) is mounted on siphunculus road.
5. the steam-cured processing system of lignite according to claim 1 or 2 or 3, it is characterised in that：It is distributed on kettle body body (2)
There are multiple sensors (16).
6. the steam-cured processing system of lignite according to claim 4, it is characterised in that：It is distributed with kettle body body (2) multiple
Sensor (16).
7. the steam-cured processing system of lignite according to claim 1 or 2 or 3, it is characterised in that：Kettle body body has perpendicular in (2)
The electrode (4) directly fixed, each electrode (4) electrically connects with the positive pole of dc source (14), and the inwall of each kettle body body (2) is straight with this
Flow the negative pole electrical connection of power supply.
8. the steam-cured processing system of lignite according to claim 6, it is characterised in that：Kettle body body has vertical fixation in (2)
Electrode (4), each electrode (4) electrically connects with the positive pole of dc source (14), each kettle body body (2) and the negative pole of the dc source
Electrical connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710558481.1A CN107227189A (en) | 2017-07-11 | 2017-07-11 | The steam-cured processing system of lignite |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710558481.1A CN107227189A (en) | 2017-07-11 | 2017-07-11 | The steam-cured processing system of lignite |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107227189A true CN107227189A (en) | 2017-10-03 |
Family
ID=59955988
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710558481.1A Pending CN107227189A (en) | 2017-07-11 | 2017-07-11 | The steam-cured processing system of lignite |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107227189A (en) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20100135851A1 (en) * | 2008-12-01 | 2010-06-03 | Estech, Llc | Waste treatment autoclave to provide for steam - assisted drying |
| CN102051246A (en) * | 2010-12-24 | 2011-05-11 | 徐斌 | Method for improving quality of brown coal |
| CN102072613A (en) * | 2011-01-20 | 2011-05-25 | 徐斌 | Method for multi-effect evaporation and dehydration of solid material |
| CN102134520A (en) * | 2011-01-28 | 2011-07-27 | 徐斌 | Method for improving quality of lignite by adopting fixed bed in single set of equipment |
| CN202660879U (en) * | 2012-06-08 | 2013-01-09 | 四川新国荣能源材料有限责任公司 | System for recycling thermal steam generated by microwave drying |
| CN204154090U (en) * | 2014-09-23 | 2015-02-11 | 中国能建集团装备有限公司北京技术中心 | brown coal drying device |
| CN206955978U (en) * | 2017-07-11 | 2018-02-02 | 云南国能清洁能源有限公司 | The steam-cured processing system of lignite |
-
2017
- 2017-07-11 CN CN201710558481.1A patent/CN107227189A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20100135851A1 (en) * | 2008-12-01 | 2010-06-03 | Estech, Llc | Waste treatment autoclave to provide for steam - assisted drying |
| CN102051246A (en) * | 2010-12-24 | 2011-05-11 | 徐斌 | Method for improving quality of brown coal |
| CN102072613A (en) * | 2011-01-20 | 2011-05-25 | 徐斌 | Method for multi-effect evaporation and dehydration of solid material |
| CN102134520A (en) * | 2011-01-28 | 2011-07-27 | 徐斌 | Method for improving quality of lignite by adopting fixed bed in single set of equipment |
| CN202660879U (en) * | 2012-06-08 | 2013-01-09 | 四川新国荣能源材料有限责任公司 | System for recycling thermal steam generated by microwave drying |
| CN204154090U (en) * | 2014-09-23 | 2015-02-11 | 中国能建集团装备有限公司北京技术中心 | brown coal drying device |
| CN206955978U (en) * | 2017-07-11 | 2018-02-02 | 云南国能清洁能源有限公司 | The steam-cured processing system of lignite |
Non-Patent Citations (1)
| Title |
|---|
| 武汉建筑材料工业学院等编: "《水泥生产机械设备》", vol. 1, 《中国建筑工业出版社》, pages: 212 * |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206955978U (en) | The steam-cured processing system of lignite | |
| CN108793074B (en) | Controllable hydrogen production device of hydrogen fuel cell | |
| CN201634674U (en) | Biphase anaerobic fermentation and acidification reaction device | |
| CN107227189A (en) | The steam-cured processing system of lignite | |
| CN203754708U (en) | Horizontal type continuous high-efficiency dry-type anaerobic fermentation device | |
| CN203079950U (en) | Small thermal-insulation fermentation tank | |
| CN206955977U (en) | The steam-cured upgrading processing unit of lignite | |
| CN111500301A (en) | Biomass fuel gas-carbon co-production line | |
| CN206953261U (en) | The steam-cured processing unit of anticorrosion | |
| CN205398550U (en) | Coal tar dewatering device | |
| CN104634073A (en) | Calcium carbonate drying device | |
| CN211726925U (en) | A dehydration fermenting installation for small-size kitchen garbage handles equipment | |
| CN211147185U (en) | Moisture-sensitive material storage and drying device | |
| CN207483734U (en) | A kind of dry-wet-coupled anaerobic reactor | |
| CN208414410U (en) | A kind of biogas fermentation device | |
| CN206291216U (en) | A kind of production equipment of high-purity normal butane | |
| CN207945484U (en) | A kind of city gas engineering system storage gas combustion apparatus | |
| CN108224935B (en) | High-temperature vacuum drying equipment and drying method for lithium ion battery powder | |
| CN102091707A (en) | Waste storage tank for dehydrating waste | |
| CN214120802U (en) | Sintering flue exhaust-heat boiler | |
| CN206953262U (en) | Vertical steam-cured kettle | |
| CN218177387U (en) | High-viscosity waste liquid relay pumping system | |
| CN215917331U (en) | Fluidized reaction system for efficiently separating biomass components | |
| CN218270084U (en) | Hot melt adhesive granule desiccator | |
| CN209720538U (en) | Dry powder temporary storage tank is used in a kind of rare earth processing technology |
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 |