CN205328879U - Sintered ceramsite apparatus for producing is used multipurposely to environment -friendly's coal gas - Google Patents
Sintered ceramsite apparatus for producing is used multipurposely to environment -friendly's coal gas Download PDFInfo
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- CN205328879U CN205328879U CN201520964858.XU CN201520964858U CN205328879U CN 205328879 U CN205328879 U CN 205328879U CN 201520964858 U CN201520964858 U CN 201520964858U CN 205328879 U CN205328879 U CN 205328879U
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- 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
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/60—Production of ceramic materials or ceramic elements, e.g. substitution of clay or shale by alternative raw materials, e.g. ashes
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Abstract
The utility model discloses a sintered ceramsite apparatus for producing is used multipurposely to environment -friendly's coal gas, including coal gas generation system, addition material prefabricated system, addition material stoving vent gas treatment system in and haydite production system. The utility model discloses can satisfy the production processes's such as raw material handling, heat source supply, finished product production, exhaust -gas treatment of fly ash sintered ceramsite production technology demand.
Description
Technical field
This utility model relates to waste emissions technical field of comprehensive utilization, is specifically related to the coal gas comprehensive utilization sintering ceramsite process units of a kind of clean environmental protection。
Background technology
From artificial lightweight haydite in 1913 after the U.S. comes out, countries in the world are according to practical situation, active development is with flyash for main raw material(s), adopt the artificial lightweight haydite substituting the non-renewable resources such as rubble, cobble that sintering process (boiler-turbine CCS, rotary kiln, sintering machine) produces, it is widely used in the building traffic industries such as high building structure, concrete component, highway, inside and outside wall board, and develops the biofilter material for administering the fields such as municipal sewage, industrial wastewater, the agricultural soil transformation of the way。
Introduce according to Ltech Corp of Britain data, the haydite of its production is used for structural concrete every cube about 20～25 pounds, higher than local rubble price 2～3 times, but due to structural light-weight concrete relatively normal concrete weight reduction 25%, drying shrinkage reduces 35%, and thermal expansion factor reduces 42%, heat conductivity reduces 62%, heatproof reaches about thousand degree, then saving entirety investment is 5～10%, therefore applies relatively common abroad。
Haydite is applied later at home, and the every annual of yield is at 4,000,000 m at the end of last century3。Major part is clay, haydites of book structure, and minority is lytag, and obtains certain achievement, such as shear wall structure House with Big Room Openning building, lake water road, Tianjin 16, No. 22 shear wall structure office buildings in Langao road, Shanghai City etc.。
In sum, sintering ceramsite of fly ash is widely used in each field due to characteristics such as its lightweight, high-strength, wear-resisting, impervious, antidetonation, sound absorption, insulations。
Utility model content
In view of this, the purpose of this utility model is in that to provide the coal gas comprehensive utilization sintering ceramsite process units of a kind of clean environmental protection, meets the process requirements of the production links such as the Feedstock treating of sintering ceramsite of fly ash production, thermal source supply, finished product production, exhaust-gas treatment。
For reaching above-mentioned purpose, this utility model provides following technical scheme:
The coal gas comprehensive utilization sintering ceramsite process units of clean environmental protection of the present utility model, dries exhaust treatment system and haydite production system including gas generating system, additive prefabrication system, additive；
Described gas generating system includes two stage type gas generating furnace, tar well, cyclone dust extractor, emergency cut-off device and stokehold water sealed tank, described two stage type gas generating furnace includes top belljar valve, top retort section body of heater, bottom gasification section body of heater and bottom ash-pan, described retort section body of heater is connected with tar well, described gasification section body of heater is connected with cyclone dust extractor, and the outlet conduit of described tar well and cyclone dust extractor introduces stokehold water sealed tank by emergency cut-off device after converging；
Described additive prefabrication system includes combustion furnace air-introduced machine, combustion furnace, additive dehydrator, additive flour mill, additive sifter and interpolation feed bin, the gas exit pipeline of described stokehold water sealed tank is connected with combustion furnace, the wind pipe of described combustion furnace air-introduced machine is connected with combustion furnace, the hot air outlet pipeline of described combustion furnace is connected with additive dehydrator, the drier outlet of described additive dehydrator is connected with additive flour mill, the powder outlet of described additive flour mill is connected with additive sifter, the powder outlet of described additive sifter is connected with adding feed bin；
Described additive is dried exhaust treatment system and is included heat exchanger, surge tank, scrubbing tower, sedimentation tank and clear water reserviors, the drying offgas outlet pipeline of described additive dehydrator is by being connected with surge tank after the hot media channel of heat exchanger, the wind pipe of described combustion furnace air-introduced machine is by being connected with combustion furnace after the cold medium channel of heat exchanger, the condensation-water drain pipeline of described heat exchanger and surge tank is connected with sedimentation tank, described sedimentation tank is connected with clear water reserviors, described clear water reserviors are connected with the spray system in scrubbing tower by circulating pump, described wash tower bottoms is connected with sedimentation tank, the offgas outlet pipeline of described surge tank is connected with scrubbing tower bottom, described scrubbing tower top is connected with toxic emission chimney；
Described haydite production system includes fine coal ash silo, weighing and dispensing system, batch mixer, stirring nucleation machine, pan-pelletizer, ceramisite sintered machine, ignition furnace air-introduced machine, ignition furnace, haydite cooler, cold air air-introduced machine, haydite disintegrating machine, haydite sifter and finished bin, described interpolation feed bin and fine coal ash silo are connected with weighing and dispensing system respectively, described weighing and dispensing system, batch mixer, stirring nucleation machine, pan-pelletizer, ceramisite sintered machine, haydite cooler, haydite disintegrating machine, haydite sifter and finished bin are sequentially connected with, the gas exit pipeline of described stokehold water sealed tank is connected with ignition furnace, the wind pipe of described ignition furnace air-introduced machine is connected with ignition furnace, described ignition furnace is connected with ceramisite sintered machine, the wind pipe of described cold air air-introduced machine is connected with haydite cooler。
Further, described gas generating system also includes drum and gas generator air-introduced machine, described gasification section body of heater is provided with water holding jacket, described drum is connected with softening grid, the water holding jacket entrance and exit of gasification section body of heater is connected with drum respectively, the steam outlet of drum is divided into two-way, and a pass enters two stage type gas generating furnace and is used as sealing gland steam, and the wind pipe of another road and gas generator air-introduced machine introduces after converging and is used as gasifying agent bottom two stage type gas generating furnace。
Further, described gas generating system also includes residual gas flashback tank and water seal feedwater piping, and industry water pipe network is connected with residual gas flashback tank, ash-pan, emergency cut-off device and stokehold water sealed tank respectively by water seal feedwater piping。
Further, described batch mixer is Double helix stir mixing machine。
Further, described stirring nucleation machine is twayblade stirring nucleation machine。
Further, described haydite cooler is rotary cooler。
Further, described haydite disintegrating machine is double-roll crusher。
Further, described haydite sifter is flat vibrating screen。
Further, between described interpolation feed bin and weighing and dispensing system, it is connected each through single-screw conveyer between fine coal ash silo and weighing and dispensing system, between weighing and dispensing system and batch mixer, between batch mixer and stirring nucleation machine and between stirring nucleation machine and pan-pelletizer。
Further, between described pan-pelletizer with ceramisite sintered machine, between ceramisite sintered machine and haydite cooler, between haydite cooler and haydite disintegrating machine, between haydite disintegrating machine and haydite sifter, it is connected each through belt conveyor between haydite sifter and finished bin。
The beneficial effects of the utility model are in that:
The coal gas comprehensive utilization sintering ceramsite process units of clean environmental protection of the present utility model includes gas generating system, additive prefabrication system, additive drying exhaust treatment system and four production units of haydite production system；The coal gas that gas generating system generates is semiwater gas, is also heating gas, does not need cooling and purifying, is respectively used to additive and dries and product sintering；Additive prefabrication system by the additive (such as gangue, mine tailings, clay) of block or pasty state is dried, grinding, obtain qualified dry powdery additive after screening；Haydite production system utilizes flyash for raw material, and additive dispensing, prepares sintering ceramsite of fly ash product through operations such as batch mixing, nucleation, balling-up, sintering, cooling, broken, screenings；Additive dries exhaust treatment system to qualified discharge after production exhaust-gas treatment。Therefore, this utility model can meet sintering ceramsite of fly ash and produce the process requirements of each link, makes full use of fly ash, turns waste into wealth。
Accompanying drawing explanation
In order to make the purpose of this utility model, technical scheme and beneficial effect clearly, this utility model provides drawings described below to illustrate:
Fig. 1 is the structural representation of gas generating system；
Fig. 2 is the structural representation of additive prefabrication system；
Fig. 3 is the structural representation that additive dries exhaust treatment system；
Fig. 4 is the structural representation of haydite production system。
Detailed description of the invention
Below in conjunction with accompanying drawing, preferred embodiment of the present utility model is described in detail。
The coal gas comprehensive utilization sintering ceramsite process units of clean environmental protection of the present utility model, dries exhaust treatment system and haydite production system including gas generating system, additive prefabrication system, additive。
Fig. 1 is the structural representation of gas generating system, as shown in the figure, gas generating system includes two stage type gas generating furnace 11, tar well 12, cyclone dust extractor 13, emergency cut-off device 14 and stokehold water sealed tank 15, described two stage type gas generating furnace 11 includes top belljar valve 111, top retort section body of heater 112, bottom gasification section body of heater 113 and bottom ash-pan 114, described retort section body of heater 112 is connected with tar well 12, described gasification section body of heater 113 is connected with cyclone dust extractor 13, the outlet conduit of described tar well 12 and cyclone dust extractor 13 introduces stokehold water sealed tank 15 by emergency cut-off device 14 after converging。
Described gas generating system also includes drum 16 and gas generator air-introduced machine 17, described gasification section body of heater 113 is provided with water holding jacket, described drum 16 is connected with softening grid 18, the water holding jacket entrance and exit of gasification section body of heater 113 is connected with drum 16 respectively, the steam outlet of drum 16 is divided into two-way, one pass enters two stage type gas generating furnace 11 and is used as sealing gland steam, and the wind pipe of another road and gas generator air-introduced machine 17 introduces after converging and is used as gasifying agent bottom two stage type gas generating furnace 11。
Described gas generating system also includes residual gas flashback tank 19 and water seal feedwater piping, and industry water pipe network 10 is connected with residual gas flashback tank 19, ash-pan 114, emergency cut-off device 14 and stokehold water sealed tank 15 respectively by water seal feedwater piping。
First coal enters two stage type gas generating furnace 11 from furnace roof coal bunker through two groups of belljar valves 111, coal dries and long low temperature distillation through fully at retort section body of heater 112, gradually form semicoke, enter gasification section body of heater 113, the gasifying agent that red-hot semicoke blasts at gasification section body of heater 113 and furnace bottom fully reacts, form coal ash through furnace reduction layer, oxide layer, grate drive and be automatically drained out from bottom ash-pan 114。
Coal, in the process of low temperature distillation, is called dry distillation gas, the top coal gas of composition two stage type gas generating furnace 11 with the coal gas that fugitive constituent precipitation is main generation, accounts for the 40% of total coal gas amount, the higher (6700kJ/Nm of its calorific value3) temperature relatively low (about 120 DEG C), and containing substantial amounts of tar。This tar formed at retort section body of heater 112 is low temperature distillation product, and its mobility is better, is collected by tar well 12 and centrally disposes。At gasification section body of heater 113, the coal gas that red-hot semicoke and gasifying agent (air, steam) generate through series of chemical such as reduction, oxidations, it is called gasification gas, the bottom coal gas of composition two stage type gas generating furnace 11, account for the 60% of total coal gas amount, the relatively low (6400kJ/Nm of its calorific value3), temperature higher (about 450 DEG C)。Because coal is at retort section body of heater 112 low temperature distillation ample time, the coal entering gasification section body of heater 113 has become semicoke, and the gasification gas therefore generated is without tar。Gasification gas forms mixed gas after cyclone dust extractor 13 dedusting and goes burning for providing thermal source through emergency cut-off device 14 and stokehold water sealed tank 15 with dry distillation gas。
Gasification section body of heater 113 being provided with water leg, the softening water in drum 16 is introduced water leg, by this self-produced steam, a steam part is used as sealing gland steam, and the air that another part introduces with gas generator air-introduced machine 17 mixes as gasifying agent。
Gas generating system is owing to have employed the hot detar technique of two section type, and the coal gas obtained is semiwater gas, is also heating gas, comparatively pure, without tar, does not need cooling and purifying。Gas composition is CO, H2、CH4, combustible component and the CO such as CnHm2、N2Etc. non-combustible composition, and in gasification the combustion adjuvant oxygen of non-complete reaction and the steam that do not decompose completely。Gas generator adopts stone coal, does not need to crush；Coal gas, for continuously generating and using, does not need gas holder to store。
Fig. 2 is the structural representation of additive prefabrication system, as shown in the figure, additive prefabrication system includes combustion furnace air-introduced machine 21, combustion furnace 22, additive dehydrator 23, additive flour mill 24, additive sifter 25 and interpolation feed bin 26, the gas exit pipeline of described stokehold water sealed tank 15 is connected with combustion furnace 22, 21 wind pipes of described combustion furnace air-introduced machine are connected with combustion furnace 22, the hot air outlet pipeline of described combustion furnace 22 is connected with additive dehydrator 23, the drier outlet of described additive dehydrator 23 is connected with additive flour mill 24, the powder outlet of described additive flour mill 24 is connected with additive sifter 25, the powder outlet of described additive sifter 25 is connected with adding feed bin 26。
The air mixed combustion that coal gas introduces with combustion furnace air-introduced machine 21 in combustion furnace 22 produces hot-air, from the hot-air of combustion furnace 22 additive (such as gangue, mine tailings, clay) with block or pasty state and flow to additive dehydrator 23 and carry out heat exchange, additive after hot-air dry flow to additive flour mill 24 from additive dehydrator 23 outlet and carries out grinding, and the additive after grinding screens out qualified dry powdery additive through additive sifter 25 and flows into interpolation feed bin 26。
Fig. 3 is the structural representation that additive dries exhaust treatment system, as shown in the figure, additive is dried exhaust treatment system and is included heat exchanger 31, surge tank 32, scrubbing tower 33, sedimentation tank 34 and clear water reserviors 35, the drying offgas outlet pipeline of described additive dehydrator 23 is by being connected with surge tank 32 after the hot media channel of heat exchanger 31, the wind pipe of described combustion furnace air-introduced machine 21 is by being connected with combustion furnace 22 after the cold medium channel of heat exchanger 31, the condensation-water drain pipeline of described heat exchanger 31 and surge tank 32 is connected with sedimentation tank 34, described sedimentation tank 34 is connected with clear water reserviors 35, described clear water reserviors 35 are connected with the spray system in scrubbing tower 33 by circulating pump 36, it is connected with sedimentation tank 34 bottom described scrubbing tower 33, the offgas outlet pipeline of described surge tank 32 is connected with scrubbing tower 33 bottom, described scrubbing tower 33 top is connected with toxic emission chimney。
The drying tail gas produced in additive prefabrication process is mainly containing additive dust, and tail gas first passes through heat exchanger 31 and carries out heat exchange with combustion furnace 22 required air；Tail gas is after air cools down, and part larger particles dust and condensed water are deposited in heat exchanger 31 and regularly discharge, and the tail gas after heat exchange enters back into surge tank 32, makes part steam condense further and take away a small amount of dust；After last tail gas entrance scrubbing tower 33 carries out cleaning dust with water, through toxic emission smoke stack emission。Slurry and scrubbing tower 33 spray washing waste water that heat exchanger 31 and surge tank 32 are got rid of are settled out sediment discharge at sedimentation tank 34, and upper strata clear water flows into clear water reserviors 35 circulated sprinkling and uses。
Fig. 4 is the structural representation of haydite production system, as shown in the figure, haydite production system includes fine coal ash silo 40, weighing and dispensing system 41, batch mixer 42, stirring nucleation machine 43, pan-pelletizer 44, ceramisite sintered machine 45, ignition furnace air-introduced machine 401, ignition furnace 402, haydite cooler 46, cold air air-introduced machine 403, haydite disintegrating machine 47, haydite sifter 48 and finished bin 49, described interpolation feed bin 26 and fine coal ash silo 40 are connected with weighing and dispensing system 41 respectively, described weighing and dispensing system 41, batch mixer 42, stirring nucleation machine 43, pan-pelletizer 44, ceramisite sintered machine 45, haydite cooler 46, haydite disintegrating machine 47, haydite sifter 48 and finished bin 49 are sequentially connected with, the gas exit pipeline of described stokehold water sealed tank 15 is connected with ignition furnace 402, the wind pipe of described ignition furnace air-introduced machine 401 is connected with ignition furnace 402, described ignition furnace 402 is connected with ceramisite sintered machine 45, the wind pipe of described cold air air-introduced machine 403 is connected with haydite cooler 46。
Described batch mixer 42 is Double helix stir mixing machine, and described stirring nucleation machine 43 stirs nucleation machine for twayblade, and described haydite cooler 46 is rotary cooler, and described haydite disintegrating machine 47 is double-roll crusher, and described haydite sifter 48 is flat vibrating screen。
It is connected each through single-screw conveyer between described interpolation feed bin 26 and weighing and dispensing system 41, between fine coal ash silo 40 and weighing and dispensing system 41, between weighing and dispensing system 41 and batch mixer 42, between batch mixer 42 and stirring nucleation machine 43 and between stirring nucleation machine 43 and pan-pelletizer 44。Between described pan-pelletizer 44 with ceramisite sintered machine 45, between ceramisite sintered machine 45 and haydite cooler 46, between haydite cooler 46 and haydite disintegrating machine 47, between haydite disintegrating machine 47 and haydite sifter 48, it is connected each through belt conveyor between haydite sifter 48 and finished bin 49。
By flyash with additive by sending into batch mixer 42 uniform stirring after weighing and dispensing system 41 accurate measurement, the stirring additional a certain amount of water wet mixing nucleation of nucleation machine 43 sent into by mixed material, wet mixed feed containing nucleus is sent into pan-pelletizer 44, and prepare the water yield according to technological requirement, carry out balling-up (according to ceramic particle technology performance, size grading adjusts the inclination angle of pan-pelletizer, angular velocity, height of baffle plate, wiper positions, inlet amount and water distribution quantity and state), again qualified raw material ball is sent into ceramisite sintered machine 45, coal gas is utilized after lighting a fire in ignition furnace 402, the raw material ball in ceramisite sintered machine 45 to be sintered, the haydite that sintering obtains is sent in haydite cooler 46, blasted air by cold air air-introduced machine 403 and carry out cooling process, last by haydite disintegrating machine 47 and haydite sifter 48 to hardening, bonding haydite crushes, sintering ceramsite of fly ash product is obtained after screening。
What finally illustrate is, preferred embodiment above is only in order to illustrate the technical solution of the utility model and unrestricted, although this utility model being described in detail by above preferred embodiment, but skilled artisan would appreciate that, in the form and details it can be made various change, without departing from this utility model claims limited range。
Claims (10)
1. the coal gas comprehensive utilization sintering ceramsite process units of a clean environmental protection, it is characterised in that: include gas generating system, additive prefabrication system, additive drying exhaust treatment system and haydite production system；
Described gas generating system includes two stage type gas generating furnace, tar well, cyclone dust extractor, emergency cut-off device and stokehold water sealed tank, described two stage type gas generating furnace includes top belljar valve, top retort section body of heater, bottom gasification section body of heater and bottom ash-pan, described retort section body of heater is connected with tar well, described gasification section body of heater is connected with cyclone dust extractor, and the outlet conduit of described tar well and cyclone dust extractor introduces stokehold water sealed tank by emergency cut-off device after converging；
Described additive prefabrication system includes combustion furnace air-introduced machine, combustion furnace, additive dehydrator, additive flour mill, additive sifter and interpolation feed bin, the gas exit pipeline of described stokehold water sealed tank is connected with combustion furnace, the wind pipe of described combustion furnace air-introduced machine is connected with combustion furnace, the hot air outlet pipeline of described combustion furnace is connected with additive dehydrator, the drier outlet of described additive dehydrator is connected with additive flour mill, the powder outlet of described additive flour mill is connected with additive sifter, the powder outlet of described additive sifter is connected with adding feed bin；
Described additive is dried exhaust treatment system and is included heat exchanger, surge tank, scrubbing tower, sedimentation tank and clear water reserviors, the drying offgas outlet pipeline of described additive dehydrator is by being connected with surge tank after the hot media channel of heat exchanger, the wind pipe of described combustion furnace air-introduced machine is by being connected with combustion furnace after the cold medium channel of heat exchanger, the condensation-water drain pipeline of described heat exchanger and surge tank is connected with sedimentation tank, described sedimentation tank is connected with clear water reserviors, described clear water reserviors are connected with the spray system in scrubbing tower by circulating pump, described wash tower bottoms is connected with sedimentation tank, the offgas outlet pipeline of described surge tank is connected with scrubbing tower bottom, described scrubbing tower top is connected with toxic emission chimney；
Described haydite production system includes fine coal ash silo, weighing and dispensing system, batch mixer, stirring nucleation machine, pan-pelletizer, ceramisite sintered machine, ignition furnace air-introduced machine, ignition furnace, haydite cooler, cold air air-introduced machine, haydite disintegrating machine, haydite sifter and finished bin, described interpolation feed bin and fine coal ash silo are connected with weighing and dispensing system respectively, described weighing and dispensing system, batch mixer, stirring nucleation machine, pan-pelletizer, ceramisite sintered machine, haydite cooler, haydite disintegrating machine, haydite sifter and finished bin are sequentially connected with, the gas exit pipeline of described stokehold water sealed tank is connected with ignition furnace, the wind pipe of described ignition furnace air-introduced machine is connected with ignition furnace, described ignition furnace is connected with ceramisite sintered machine, the wind pipe of described cold air air-introduced machine is connected with haydite cooler。
2. the coal gas comprehensive utilization sintering ceramsite process units of clean environmental protection according to claim 1, it is characterized in that: described gas generating system also includes drum and gas generator air-introduced machine, described gasification section body of heater is provided with water holding jacket, described drum is connected with softening grid, the water holding jacket entrance and exit of gasification section body of heater is connected with drum respectively, the steam outlet of drum is divided into two-way, one pass enters two stage type gas generating furnace and is used as sealing gland steam, the wind pipe of another road and gas generator air-introduced machine introduces after converging and is used as gasifying agent bottom two stage type gas generating furnace。
3. the coal gas comprehensive utilization sintering ceramsite process units of clean environmental protection according to claim 1, it is characterized in that: described gas generating system also includes residual gas flashback tank and water seal feedwater piping, industry water pipe network is connected with residual gas flashback tank, ash-pan, emergency cut-off device and stokehold water sealed tank respectively by water seal feedwater piping。
4. the coal gas comprehensive utilization sintering ceramsite process units of clean environmental protection according to claim 1, it is characterised in that: described batch mixer is Double helix stir mixing machine。
5. the coal gas comprehensive utilization sintering ceramsite process units of clean environmental protection according to claim 1, it is characterised in that: described stirring nucleation machine is twayblade stirring nucleation machine。
6. the coal gas comprehensive utilization sintering ceramsite process units of clean environmental protection according to claim 1, it is characterised in that: described haydite cooler is rotary cooler。
7. the coal gas comprehensive utilization sintering ceramsite process units of clean environmental protection according to claim 1, it is characterised in that: described haydite disintegrating machine is double-roll crusher。
8. the coal gas comprehensive utilization sintering ceramsite process units of clean environmental protection according to claim 1, it is characterised in that: described haydite sifter is flat vibrating screen。
9. the coal gas comprehensive utilization sintering ceramsite process units of clean environmental protection according to claim 1, it is characterised in that: it is connected each through single-screw conveyer between described interpolation feed bin and weighing and dispensing system, between fine coal ash silo and weighing and dispensing system, between weighing and dispensing system and batch mixer, between batch mixer and stirring nucleation machine and between stirring nucleation machine and pan-pelletizer。
10. the coal gas comprehensive utilization sintering ceramsite process units of clean environmental protection according to claim 1, it is characterised in that: between described pan-pelletizer with ceramisite sintered machine, between ceramisite sintered machine and haydite cooler, between haydite cooler and haydite disintegrating machine, between haydite disintegrating machine and haydite sifter, it is connected each through belt conveyor between haydite sifter and finished bin。
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520964858.XU CN205328879U (en) | 2015-11-27 | 2015-11-27 | Sintered ceramsite apparatus for producing is used multipurposely to environment -friendly's coal gas |
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| CN201520964858.XU CN205328879U (en) | 2015-11-27 | 2015-11-27 | Sintered ceramsite apparatus for producing is used multipurposely to environment -friendly's coal gas |
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| CN205328879U true CN205328879U (en) | 2016-06-22 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108264252A (en) * | 2018-01-11 | 2018-07-10 | 晋中市祁宏粉煤灰科技开发有限公司 | A kind of box positive pressure sintering ceramsite of fly ash production line of green |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108264252A (en) * | 2018-01-11 | 2018-07-10 | 晋中市祁宏粉煤灰科技开发有限公司 | A kind of box positive pressure sintering ceramsite of fly ash production line of green |
| CN108264252B (en) * | 2018-01-11 | 2023-09-08 | 晋中市祁宏粉煤灰科技开发有限公司 | Green box-type positive pressure fly ash sintered ceramsite production line |
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Granted publication date: 20160622 Termination date: 20161127 |