CN204454921U - Manganese slag production of compound fertilizer device - Google Patents
Manganese slag production of compound fertilizer device Download PDFInfo
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- CN204454921U CN204454921U CN201420756164.2U CN201420756164U CN204454921U CN 204454921 U CN204454921 U CN 204454921U CN 201420756164 U CN201420756164 U CN 201420756164U CN 204454921 U CN204454921 U CN 204454921U
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- manganese slag
- roasting kiln
- compound fertilizer
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- washing tower
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Abstract
The utility model discloses a kind of manganese slag production of compound fertilizer device, comprise gas generating system, manganese slag prefabrication system, manganese slag dries exhaust treatment system, production of compound fertilizer system and mixed fertilizer drying cooled exhaust gas treatment system, gas generating system comprises two stage type gas generating furnace, tar well, tornado dust collector and stokehold water-sealed tank, manganese slag prefabrication system comprises roasting kiln induced draft fan I, roasting kiln I, manganese slag dryer, acidified modified device and neutralization reactor, manganese slag is dried exhaust treatment system and is comprised interchanger, surge tank, washing tower I, settling tank I and clean water basin I, production of compound fertilizer system comprises roasting kiln induced draft fan II, roasting kiln II, weighing and dispensing system, mixer, raw material chopper, tablets press, mixed fertilizer drying machine and compound fertilizer cooler provided, mixed fertilizer drying cooled exhaust gas treatment system comprises settling pocket, washing tower II, settling tank II and clean water basin II.The utility model solves manganese dregs reject emission problem, makes full use of resource, turns waste into wealth.
Description
Technical field
The utility model relates to waste emissions technical field of comprehensive utilization, is specifically related to a kind of manganese slag production of compound fertilizer device.
Background technology
Potassium permanganate production can produce a large amount of waste emissions-manganese slag, although manganese slag belongs to trade waste, discarded bank up that not even a blade of grass grows at place, leach liquor is amaranth, direct serious environment pollution.But its composition structure of manganese slag is all inorganic mineral, containing the direct available macronutrient of plant in analysis of experiments manganese slag, potassium (K
2o), phosphorus (P
2o
5) contents on dry basis is up to 10 ~ 11%.Except containing except the potassium needed for plant-growth in manganese slag, also there is the oxidizing species potassium permanganate be harmful to crop growth, simultaneously due to containing KOH, making manganese slag pH value higher, is the reason that manganese slag can not be directly agricultural.
For the oxidizing species potassium permanganate existed in manganese slag and alkaline matter KOH, pyrolytic decomposition and phosphoric acid neutralizing treatment mode is taked to carry out modification to it.
Potassium permanganate resolves into potassium manganate, MnO at 240 DEG C
2and oxygen, potassium manganate can decompose generation MnO further
2and oxygen, reaction formula is as follows:
2KMnO
4—→K
2MnO
4+MnO
2+O
2
2K
2MnO
4—→2K
2O+2MnO
2+O
2↑
Thus potassium permanganate harmful in manganese slag is changed into the nutrient K produced needed for Chemical Mixed Fertilizer
2o.
For the KOH in manganese slag, carry out neutralization reaction adjust ph by adding phosphoric acid:
H
3PO
4+3KOH
—→
K
3PO
4+3H
2O
By above modification, after modification is passed through for the objectionable impurities potassium permanganate in manganese slag and KOH, generate the K produced needed for Chemical Mixed Fertilizer
2o and K
3pO
4, make manganese slag meet production of compound fertilizer requirement, can not work the mischief to farm crop and soil.
Therefore, as raw material production Chemical Mixed Fertilizer after manganese slag modification, not only solve the emission problem of existing waste, and production cost like product more of the same trade can reduce by more than 100 yuan/ton, is make full use of resource, really accomplishes to turn waste into wealth.
Utility model content
In view of this, the purpose of this utility model is to provide a kind of manganese slag production of compound fertilizer device, meets the process requirements of the production links such as the Feedstock treating of manganese slag production of compound fertilizer, thermal source supply, finished product production, off gas treatment.
For achieving the above object, the utility model provides following technical scheme:
Manganese slag production of compound fertilizer device of the present utility model, comprises gas generating system, manganese slag prefabrication system, the oven dry of manganese slag exhaust treatment system, production of compound fertilizer system and mixed fertilizer drying cooled exhaust gas treatment system;
Described gas generating system comprises two stage type gas generating furnace, tar well, tornado dust collector, emergency switching-off device and stokehold water-sealed tank, described two stage type gas generating furnace comprises 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 tornado dust collector, introduces stokehold water-sealed tank after the outlet conduit of described tar well and tornado dust collector converges by emergency switching-off device;
Described manganese slag prefabrication system comprises roasting kiln induced draft fan I, roasting kiln I, manganese slag dryer, acidified modified device and neutralization reactor, the gas exit pipeline of described stokehold water-sealed tank is connected with roasting kiln I, the wind pipe of described roasting kiln induced draft fan I is connected with roasting kiln I, the hot air outlet pipeline of described roasting kiln I is connected with manganese slag dryer, the dry manganese slag outlet of described manganese slag dryer is connected with acidified modified device, and the acidifying manganese slag outlet of described acidified modified device is connected with neutralization reactor;
Described manganese slag is dried exhaust treatment system and is comprised interchanger, surge tank, washing tower I, settling tank I and clean water basin I, the oven dry offgas outlet pipeline of described manganese slag dryer is by being connected with surge tank after the hot media channel of interchanger, the wind pipe of described roasting kiln induced draft fan I is by being connected with roasting kiln I after the cold medium channel of interchanger, described interchanger is connected with settling tank I with the condensation-water drain pipeline of surge tank, described settling tank I is connected with clean water basin I, described clean water basin I are connected with the sprinkling system in washing tower I by recycle pump I, be connected with settling tank I bottom described washing tower I, the offgas outlet pipeline of described surge tank is connected with washing tower I bottom, described washing tower I top is connected with exhaust gas emission chimney,
Described production of compound fertilizer system comprises roasting kiln induced draft fan II, roasting kiln II, weighing and dispensing system, mixer, raw material chopper, tablets press, mixed fertilizer drying machine, compound fertilizer cooler provided, freezing air induced draft fan, sieve apparatus, film applicator and metering packaging machine, described weighing and dispensing system, mixer, raw material chopper, tablets press, mixed fertilizer drying machine, compound fertilizer cooler provided, sieve apparatus, film applicator is connected successively with metering packaging machine, the gas exit pipeline of described stokehold water-sealed tank is connected with roasting kiln II, the wind pipe of described roasting kiln induced draft fan II is connected with roasting kiln II, the hot air outlet pipeline of described roasting kiln II is connected with mixed fertilizer drying machine, the wind pipe of described freezing air induced draft fan is connected with compound fertilizer cooler provided,
Described mixed fertilizer drying cooled exhaust gas treatment system comprises settling pocket, washing tower II, settling tank II and clean water basin II, oven dry offgas outlet pipeline and the cooled exhaust gas outlet conduit of compound fertilizer cooler provided of described mixed fertilizer drying machine converge and are connected with settling pocket afterwards, the offgas outlet pipeline of described settling pocket is connected with washing tower II bottom, described washing tower II top is connected with exhaust gas emission chimney, described clean water basin II are connected with tap water pipe network, described clean water basin II are connected with the sprinkling system in washing tower II by recycle pump II, be connected with settling tank II bottom described washing tower II, described settling tank II is connected with clean water basin II.
Further, described gas generating system also comprises drum and producer gas generator induced draft fan, described gasification section body of heater is provided with water holding jacket, described drum is connected with softening water pipe network, 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 producer gas generator induced draft fan converges bottom rear introducing two stage type gas generating furnace as vaporized chemical.
Further, described gas generating system also comprises residual gas flashback tank and water seal feedwater piping, and service water pipe network is connected with residual gas flashback tank, ash-pan, emergency switching-off device and stokehold water-sealed tank respectively by water seal feedwater piping.
Further, described interchanger is shell and tube heat exchanger, and hot media channel is shell side passage, and cold medium channel is tube side passage.
Further; described sieve apparatus is made up of upper strata scalping, middle level dusting cover and lower floor's powder plate; the Chemical Mixed Fertilizer outlet of described compound fertilizer cooler provided is connected with the upper strata scalping of sieve apparatus; the middle level dusting cover of described sieve apparatus is connected with film applicator; the upper strata scalping of described sieve apparatus is connected with raw material chopper, and lower floor's powder plate of described sieve apparatus is connected with tablets press.
The beneficial effects of the utility model are:
Manganese slag production of compound fertilizer device of the present utility model comprises gas generating system, manganese slag prefabrication system, the oven dry of manganese slag exhaust treatment system, production of compound fertilizer system and mixed fertilizer drying cooled exhaust gas treatment system five productive units; The coal gas that gas generating system generates is semi-water gas, is also heating gas, does not need cooling and purifying, is respectively used to manganese slag and product oven dry; Manganese slag prefabrication system, to the objectionable impurities potassium permanganate in manganese slag and KOH modification, generates the K produced needed for Chemical Mixed Fertilizer
2o and K
3pO
4, make manganese slag meet production of compound fertilizer requirement; Production of compound fertilizer system utilizes manganese slag for raw material, and by adding various nitrogen, phosphorus, potassium base fertilizer obtain compound fertilizer product; Manganese slag oven dry exhaust treatment system and mixed fertilizer drying cooled exhaust gas treatment system are to qualified discharge after process gas process.Therefore, the utility model can meet the process requirements of each link of manganese slag production of compound fertilizer, not only solves the emission problem of existing waste, and makes full use of resource, turn waste into wealth.
Accompanying drawing explanation
In order to make the purpose of this utility model, technical scheme and beneficial effect clearly, the utility model provides following accompanying drawing to be described:
Fig. 1 is the structural representation of gas generating system;
Fig. 2 is the structural representation of manganese slag prefabrication system;
Fig. 3 is the structural representation that manganese slag dries exhaust treatment system;
Fig. 4 is the structural representation of production of compound fertilizer system;
Fig. 5 is the structural representation of mixed fertilizer drying cooled exhaust gas treatment system.
Embodiment
Below in conjunction with accompanying drawing, preferred embodiment of the present utility model is described in detail.
Manganese slag production of compound fertilizer device of the present utility model, comprises gas generating system, manganese slag prefabrication system, the oven dry of manganese slag exhaust treatment system, production of compound fertilizer system and mixed fertilizer drying cooled exhaust gas treatment system.
Fig. 1 is the structural representation of gas generating system, as shown in the figure, gas generating system comprises two stage type gas generating furnace 11, tar well 12, tornado dust collector 13, emergency switching-off device 14 and stokehold water-sealed tank 15, described two stage type gas generating furnace 11 comprises 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 tornado dust collector 13, stokehold water-sealed tank 15 is introduced by emergency switching-off device 14 after the outlet conduit of described tar well 12 and tornado dust collector 13 converges.
Described gas generating system also comprises drum 16 and producer gas generator induced draft fan 17, described gasification section body of heater 113 is provided with water holding jacket, described drum 16 is connected with softening water pipe network 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 producer gas generator induced draft fan 17 converges bottom rear introducing two stage type gas generating furnace 11 as vaporized chemical.
Described gas generating system also comprises residual gas flashback tank 19 and water seal feedwater piping, and service water pipe network 10 is connected with residual gas flashback tank 19, ash-pan 114, emergency switching-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 at retort section body of heater 112 through sufficient drying and long low-temperature pyrolysis, form semicoke gradually, enter gasification section body of heater 113, the vaporized chemical that red-hot semicoke blasts at gasification section body of heater 113 and furnace bottom fully reacts, through furnace reduction layer, zone of oxidation and form coal ash, driven by grate and automatically discharge from bottom ash-pan 114.
Coal is in the process of low-temperature pyrolysis, and with fugitive constituent precipitation for the coal gas of main generation is called dry distillation gas, the top coal gas of composition two stage type gas generating furnace 11, accounts for 40% of total coal gas amount, the higher (6700kJ/Nm of its calorific value
3) temperature lower (about 120 DEG C), and containing a large amount of tar.This tar formed at retort section body of heater 112 is low-temperature pyrolysis product, and its mobility is better, is collected centrally dispose by tar well 12.At gasification section body of heater 113, the coal gas that red-hot semicoke and vaporized chemical (air, water vapor) generate through series of chemical such as reduction, oxidations, be called gasification gas, the bottom coal gas of composition two stage type gas generating furnace 11, account for 60% of total coal gas amount, the relatively low (6400kJ/Nm of its calorific value
3), temperature higher (about 450 DEG C).Because coal is at retort section body of heater 112 low-temperature pyrolysis ample time, the coal entering gasification section body of heater 113 becomes semicoke, and the gasification gas therefore generated is not containing tar.Gasification gas forms mixed gas and goes to burn for providing thermal source through emergency switching-off device 14 and stokehold water-sealed tank 15 after tornado dust collector 13 dedusting with dry distillation gas.
Gasification section body of heater 113 is provided with water jacket, the softening water in drum 16 is introduced water jacket, by this self-produced water vapor, a water vapor part is used as sealing gland steam, and the air mixed that another part and producer gas generator induced draft fan 17 are introduced is used as vaporized chemical.
Gas generating system is owing to have employed the hot detar technique of two section type, and the coal gas obtained is semi-water gas, is also heating gas, comparatively pure, not containing tar, does not need cooling and purifying.Gas composition is CO, H
2, CH
4, combustiblecomponents and the CO such as CnHm
2, N
2etc. non-combustible composition, and in gasification the ignition dope oxygen of non-complete reaction and the water vapor that do not decompose completely.Producer gas generator adopts stone coal, does not need fragmentation; Coal gas is produce continuously and use, and does not need gas holder to store.
Fig. 2 is the structural representation of manganese slag prefabrication system, as shown in the figure, manganese slag prefabrication system comprises roasting kiln induced draft fan I 21, roasting kiln I 22, manganese slag dryer 23, acidified modified device 24 and neutralization reactor 25, the gas exit pipeline of described stokehold water-sealed tank 15 is connected with roasting kiln I 22, the wind pipe of described roasting kiln induced draft fan I 21 is connected with roasting kiln I 22, the hot air outlet pipeline of described roasting kiln I 22 is connected with manganese slag dryer 23, the dry manganese slag outlet of described manganese slag dryer 23 is connected with acidified modified device 24, the acidifying manganese slag outlet of described acidified modified device 24 is connected with neutralization reactor 25.
Described manganese slag dryer 23 is roller drying machine, and described acidified modified device 24 is vertical mixing crusher, and described neutralization reactor 25 stacks retort for leaving standstill.
The dry manganese slag outlet of described manganese slag dryer 23 is connected with acidified modified device 24 by rotary conveyor.
The air mixed that coal gas is introduced with roasting kiln induced draft fan I 21 in roasting kiln I 22 is burnt and is produced warm air, flow to manganese slag dryer 23 carry out heat exchange from the warm air of roasting kiln I 22 and manganese slag raw material, manganese slag after hot-air dry flows out from the outlet of manganese slag dryer 23, deliver to acidified modified device 24 phosphoric acid through rotary conveyor and carry out acidified modified process, pH value is adjusted to 7 ~ 8, and further mixing is carried out with broken to material, material after fragmentation flows into neutralization reactor 25 and leaves standstill one day, and making it fully react becomes qualified prefabricated manganese slag.
Manganese slag prefabrication system, for the oxidizing species potassium permanganate existed in manganese slag and alkaline matter KOH, takes pyrolytic decomposition and phosphoric acid neutralizing treatment mode to carry out modification to it.Potassium permanganate pyrolytic decomposition changes into the nutrient K produced needed for Chemical Mixed Fertilizer
2o, the phosphoric acid added and KOH carry out neutralization reaction and generate phosphorus potash fertilizer K
3pO
4, make manganese slag meet production of compound fertilizer requirement, can not work the mischief to farm crop and soil.
Fig. 3 is the structural representation that manganese slag dries exhaust treatment system, as shown in the figure, manganese slag is dried exhaust treatment system and is comprised interchanger 31, surge tank 32, washing tower I 33, settling tank I 34 and clean water basin I 35, the oven dry offgas outlet pipeline of described manganese slag dryer 23 is by being connected with surge tank 32 after the hot media channel of interchanger 31, the wind pipe of described roasting kiln induced draft fan I 21 is by being connected with roasting kiln I 22 after the cold medium channel of interchanger 31, described interchanger 31 is connected with settling tank I 34 with the condensation-water drain pipeline of surge tank 32, described settling tank I 34 is connected with clean water basin I 35, described clean water basin I 35 are connected with the sprinkling system in washing tower I 33 by recycle pump I 36, be connected with settling tank I 34 bottom described washing tower I 33, the offgas outlet pipeline of described surge tank 32 is connected with washing tower I 33 bottom, described washing tower I 33 top is connected with exhaust gas emission chimney.
Described interchanger 31 is shell and tube heat exchanger, and hot media channel is shell side passage, and cold medium channel is tube side passage.Described settling tank I 34 is two-stage settling tank, and upper level settling tank is connected with next stage settling tank by overflow port.Described washing tower I 33 is packing tower.
The oven dry tail gas produced in manganese slag prefabrication process is mainly containing manganese slag dust, and first tail gas carry out heat exchange by interchanger 31 and roasting kiln I 22 required air; Tail gas is after air cooling, and part larger particles dust and water of condensation are deposited on 31 also regularly discharges in interchanger, and the tail gas after heat exchange enters surge tank 32 again, makes the part further condensation of water vapor and takes away a small amount of dust; Last tail gas enters after washing tower I 33 water carries out scrubbing dust collection, through exhaust gas emission smoke stack emission.The slag slurry that interchanger 31 and surge tank 32 are got rid of and washing tower I 33 spray washing waste water are settled out sediment discharge at settling tank I 34, and upper strata clear water flows into clean water basin I 35 circulated sprinkling and uses.
Fig. 4 is the structural representation of production of compound fertilizer system, as shown in the figure, production of compound fertilizer system comprises roasting kiln induced draft fan II 401, roasting kiln II 40, weighing and dispensing system 41, mixer 42, raw material chopper 43, tablets press 44, mixed fertilizer drying machine 45, compound fertilizer cooler provided 46, freezing air induced draft fan 402, sieve apparatus 47, film applicator 48 and metering packaging machine 49, described weighing and dispensing system 41, mixer 42, raw material chopper 43, tablets press 44, mixed fertilizer drying machine 45, compound fertilizer cooler provided 46, sieve apparatus 47, film applicator 48 is connected successively with metering packaging machine 49, the gas exit pipeline of described stokehold water-sealed tank 15 is connected with roasting kiln II 40, the wind pipe of described roasting kiln induced draft fan II 401 is connected with roasting kiln II 40, the hot air outlet pipeline of described roasting kiln II 40 is connected with mixed fertilizer drying machine 45, the wind pipe of described freezing air induced draft fan 402 is connected with compound fertilizer cooler provided 46.
Described mixer 42 is with between raw material chopper 43, be all connected by rotary conveyor between raw material chopper 43 with tablets press 44 and between tablets press 44 with mixed fertilizer drying machine 45.Described mixed fertilizer drying machine 45 is with between compound fertilizer cooler provided 46, be all connected by lift between compound fertilizer cooler provided 46 with sieve apparatus 47, between sieve apparatus 47 with film applicator 48 and between film applicator 48 with metering packaging machine 49.
Described tablets press 44 is rotary drum granulator, and described mixed fertilizer drying machine 45 is rotary dryer, and described compound fertilizer cooler provided 46 is rotary cooler.
Described sieve apparatus 47 is made up of upper strata scalping, middle level dusting cover and lower floor's powder plate; the Chemical Mixed Fertilizer outlet of described compound fertilizer cooler provided 46 is connected with the upper strata scalping of sieve apparatus 47; the middle level dusting cover of described sieve apparatus 47 is connected with film applicator 48; the upper strata scalping of described sieve apparatus 47 is connected with raw material chopper 43, and lower floor's powder plate of described sieve apparatus 47 is connected with tablets press 44.
By prefabricated manganese slag and various nitrogen, phosphorus, potassium base fertilizer (Repone K, phosphorus ammonium, urea, ammonium chloride and wilkinite etc.) by sending into mixer 42 uniform stirring after weighing and dispensing system 41 accurate measurement; mixed material is sent into raw material chopper 43 and is carried out fragmentation, and after broken, tablets press 44 sent into by material.Although the material major part after granulation forms particle, but now pellet moisture is high, intensity is low, the requirement of packed and transported cannot be met, work in-process after granulating and forming send into mixed fertilizer drying machine 45, the air mixed that coal gas is introduced with roasting kiln induced draft fan II 401 in roasting kiln II 40 is burnt and is produced warm air, carries out drying and processing from roasting kiln II 40 warm air out to the material in mixed fertilizer drying machine 45.After drying, temperature of charge is higher, sends into compound fertilizer cooler provided 46, blasts air carry out cooling process by freezing air induced draft fan 402, improves granule strength further, reduces moisture.Cooling after material send into sieve apparatus 47 carry out airtight sub-sieve, macrobead returning charge sieve with dusting cover after raw material chopper 43 fragmentation under fine powder jointly return tablets press 44, again participate in granulation process, so circulate.The qualified work in-process sifted out are sent into film applicator 48 by lift and are carried out coating problems, and after film, finished product sends into metering packaging machine 49 metering packing by lift, obtains compound fertilizer product.
Fig. 5 is the structural representation of mixed fertilizer drying cooled exhaust gas treatment system, as shown in the figure, mixed fertilizer drying cooled exhaust gas treatment system comprises settling pocket 51, washing tower II 52, settling tank II 53 and clean water basin II 54, oven dry offgas outlet pipeline and the cooled exhaust gas outlet conduit of compound fertilizer cooler provided 46 of described mixed fertilizer drying machine 45 converge and are connected with settling pocket 51 afterwards, the offgas outlet pipeline of described settling pocket 51 is connected with washing tower II 52 bottom, described washing tower II 52 top is connected with exhaust gas emission chimney, described clean water basin II 54 are connected with tap water pipe network 55, described clean water basin II 54 are connected with the sprinkling system in washing tower II 52 by recycle pump II 56, be connected with settling tank II 53 bottom described washing tower II 52, described settling tank II 53 is connected with clean water basin II 54.
Described settling pocket 51 is gravity settling chamber; Described settling tank II 53 is two-stage settling tank, and upper level settling tank is connected with next stage settling tank by overflow port; Described washing tower II 52 is packing tower.
Mixed fertilizer drying tail gas and Chemical Mixed Fertilizer cooled exhaust gas share a set of exhaust treatment system, and mixed fertilizer drying cooled exhaust gas is mainly containing Chemical Mixed Fertilizer dust, SO
2with a small amount of ammonia, first tail gas remove larger particles dust by settling pocket 51, then enter washing tower II 52 water and carry out spray washing, and except can further except dedusting, can play desulfurization and the effect except ammonia, the tail gas after process be through exhaust gas emission smoke stack emission simultaneously.Washing tower II 52 spray washing waste water is settled out sediment discharge at settling tank II 53, and upper strata clear water flows into clean water basin II 54 circulated sprinkling and uses.
What finally illustrate is, above preferred embodiment is only in order to illustrate the technical solution of the utility model and unrestricted, although be described in detail the utility model by above preferred embodiment, but those skilled in the art are to be understood that, various change can be made to it in the form and details, and not depart from the utility model claims limited range.
Claims (5)
1. a manganese slag production of compound fertilizer device, is characterized in that: comprise gas generating system, manganese slag prefabrication system, the oven dry of manganese slag exhaust treatment system, production of compound fertilizer system and mixed fertilizer drying cooled exhaust gas treatment system;
Described gas generating system comprises two stage type gas generating furnace, tar well, tornado dust collector, emergency switching-off device and stokehold water-sealed tank, described two stage type gas generating furnace comprises 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 tornado dust collector, introduces stokehold water-sealed tank after the outlet conduit of described tar well and tornado dust collector converges by emergency switching-off device;
Described manganese slag prefabrication system comprises roasting kiln induced draft fan I, roasting kiln I, manganese slag dryer, acidified modified device and neutralization reactor, the gas exit pipeline of described stokehold water-sealed tank is connected with roasting kiln I, the wind pipe of described roasting kiln induced draft fan I is connected with roasting kiln I, the hot air outlet pipeline of described roasting kiln I is connected with manganese slag dryer, the dry manganese slag outlet of described manganese slag dryer is connected with acidified modified device, and the acidifying manganese slag outlet of described acidified modified device is connected with neutralization reactor;
Described manganese slag is dried exhaust treatment system and is comprised interchanger, surge tank, washing tower I, settling tank I and clean water basin I, the oven dry offgas outlet pipeline of described manganese slag dryer is by being connected with surge tank after the hot media channel of interchanger, the wind pipe of described roasting kiln induced draft fan I is by being connected with roasting kiln I after the cold medium channel of interchanger, described interchanger is connected with settling tank I with the condensation-water drain pipeline of surge tank, described settling tank I is connected with clean water basin I, described clean water basin I are connected with the sprinkling system in washing tower I by recycle pump I, be connected with settling tank I bottom described washing tower I, the offgas outlet pipeline of described surge tank is connected with washing tower I bottom, described washing tower I top is connected with exhaust gas emission chimney,
Described production of compound fertilizer system comprises roasting kiln induced draft fan II, roasting kiln II, weighing and dispensing system, mixer, raw material chopper, tablets press, mixed fertilizer drying machine, compound fertilizer cooler provided, freezing air induced draft fan, sieve apparatus, film applicator and metering packaging machine, described weighing and dispensing system, mixer, raw material chopper, tablets press, mixed fertilizer drying machine, compound fertilizer cooler provided, sieve apparatus, film applicator is connected successively with metering packaging machine, the gas exit pipeline of described stokehold water-sealed tank is connected with roasting kiln II, the wind pipe of described roasting kiln induced draft fan II is connected with roasting kiln II, the hot air outlet pipeline of described roasting kiln II is connected with mixed fertilizer drying machine, the wind pipe of described freezing air induced draft fan is connected with compound fertilizer cooler provided,
Described mixed fertilizer drying cooled exhaust gas treatment system comprises settling pocket, washing tower II, settling tank II and clean water basin II, oven dry offgas outlet pipeline and the cooled exhaust gas outlet conduit of compound fertilizer cooler provided of described mixed fertilizer drying machine converge and are connected with settling pocket afterwards, the offgas outlet pipeline of described settling pocket is connected with washing tower II bottom, described washing tower II top is connected with exhaust gas emission chimney, described clean water basin II are connected with tap water pipe network, described clean water basin II are connected with the sprinkling system in washing tower II by recycle pump II, be connected with settling tank II bottom described washing tower II, described settling tank II is connected with clean water basin II.
2. manganese slag production of compound fertilizer device according to claim 1, it is characterized in that: described gas generating system also comprises drum and producer gas generator induced draft fan, described gasification section body of heater is provided with water holding jacket, described drum is connected with softening water pipe network, 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, and the wind pipe of another road and producer gas generator induced draft fan converges bottom rear introducing two stage type gas generating furnace as vaporized chemical.
3. manganese slag production of compound fertilizer device according to claim 1, it is characterized in that: described gas generating system also comprises residual gas flashback tank and water seal feedwater piping, service water pipe network is connected with residual gas flashback tank, ash-pan, emergency switching-off device and stokehold water-sealed tank respectively by water seal feedwater piping.
4. manganese slag production of compound fertilizer device according to claim 1, it is characterized in that: described interchanger is shell and tube heat exchanger, hot media channel is shell side passage, and cold medium channel is tube side passage.
5. manganese slag production of compound fertilizer device according to claim 1; it is characterized in that: described sieve apparatus is made up of upper strata scalping, middle level dusting cover and lower floor's powder plate; the Chemical Mixed Fertilizer outlet of described compound fertilizer cooler provided is connected with the upper strata scalping of sieve apparatus; the middle level dusting cover of described sieve apparatus is connected with film applicator; the upper strata scalping of described sieve apparatus is connected with raw material chopper, and lower floor's powder plate of described sieve apparatus is connected with tablets press.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420756164.2U CN204454921U (en) | 2014-12-05 | 2014-12-05 | Manganese slag production of compound fertilizer device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420756164.2U CN204454921U (en) | 2014-12-05 | 2014-12-05 | Manganese slag production of compound fertilizer device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204454921U true CN204454921U (en) | 2015-07-08 |
Family
ID=53661834
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420756164.2U Expired - Fee Related CN204454921U (en) | 2014-12-05 | 2014-12-05 | Manganese slag production of compound fertilizer device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204454921U (en) |
-
2014
- 2014-12-05 CN CN201420756164.2U patent/CN204454921U/en not_active Expired - Fee Related
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