CN202610084U - Pulse combustion inner heated fluidized bed sludge-drying system - Google Patents
Pulse combustion inner heated fluidized bed sludge-drying system Download PDFInfo
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- CN202610084U CN202610084U CN 201220277672 CN201220277672U CN202610084U CN 202610084 U CN202610084 U CN 202610084U CN 201220277672 CN201220277672 CN 201220277672 CN 201220277672 U CN201220277672 U CN 201220277672U CN 202610084 U CN202610084 U CN 202610084U
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- fluidized bed
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Abstract
The utility model relates to a pulse combustion inner heated fluidized bed sludge-drying system. The pulse combustion inner heated fluidized bed sludge-drying system comprises a pulse combustor, a wet sludge feeding pelleting device, an inner heated fluidized bed dryer, a dust-removing device and a deodorization device, wherein a tail pipe of the pulse combustor is connected with an air inlet of the inner heated fluidized bed dryer, a feed port of the inner heated fluidized bed dryer is connected with the wet sludge feeding pelleting device, an air outlet of the inner heated fluidized bed dryer is connected with the dust-removing device, and the dust-removing device is further connected with the deodorization device. The pulse combustion inner heated fluidized bed sludge-drying system utilizes the technology combining pulse combustion and a inner heated fluidized bed to dry sludge, improves drying intensity, lowers energy consumption, reduces treatment quantity of off-gas, and reduces oxygen content of the system, and is free of dangers of dust combustion and explosion, safe and reliable.
Description
Technical field
The utility model has been announced a kind of internal heating fluidized bed system of intermittent combustion that is used for drying sludge.
Background technology
The mud generation is big, instability, foul smelling, contain hazardous and noxious substances such as pathogenic micro-organism, if without suitably handle get into environment after, can bring secondary pollution to water body and atmosphere.Therefore, the purpose of sludge treatment and disposal and the governing principle that will follow are " minimizing, stabilization, innoxious and resource utilizations ".Reach " Four Modernizations " of above requirement, it is crucial removing moisture.After traditional concentration and dewatering process processing, the water ratio of mud can not reach below 60%, and economic mechanical dehydration moisture content of the cake is about 75%.Reach deep dehydration, need to introduce dry technology commonly used in the chemical industry operation mud.
At present, the most common, sophisticated drying sludge technology is a mud heated drying technology.Whether contact with mud according to thermal medium, existing mud heated drying technology: direct heat dry technology, indirect thermal dry technology and direct-indirect combined formula dry technology if can be divided three classes.The essence of direct heat dry technology is the utilization of convection drying technology; The hot gas that is about to the combustion chamber generation directly contacts mixing with mud; Make mud be able to heating; Moisture is able to evaporation and finally obtains the dewatered sludge product, and representational drying cartridge is equipped with revolver drier, spray-type drier, belt dryer, Flash Type moisture eliminator, volution formula moisture eliminator etc.Its advantage is that technical process is simple, the unit treatment capacity is big, is prone to industriallization, and weak point is that production unit is huge, and floor space is big; Time of drying is long; Must could discharge after the deodorizing in the tail gas, and the thermosteresis of exhaust emissions is also very big, whole drying process economy is relatively poor.
Contact drying is exactly in fact a conductive drying; Be about to the hot gas that roasting kiln produces and transmit through steam, deep fat medium, the heating wall, thus the wet mud of wall opposite side is heated, moisture evaporation and removing; Operating equipment has the film heat drier, disc type heat drier etc.Its advantage is that drying efficiency is high, the danger of not having blast and catching fire, and the exhaust emissions amount is little; Working cost is lower, whole drying process better economy, and weak point is that drying process and equipment are all complicated; The unit treatment capacity is less, and is prone to sticking wall, and is inapplicable to the mud that adhesivity is big.
Directly-and indirect combined formula dehumidification system then is the integration of convection current-conduction technique, and it has concurrently directly and the technological advantage of contact drying, and development potentiality is huge.Representative device such as Vomm designed high speed film drier, also there are shortcomings such as energy consumption is big, sticking problem is serious in the belt dryer that the novel fluidized bed moisture eliminator of Sulzer exploitation and Envirex release etc.Therefore, exploitation cuts down the consumption of energy, reduces the adherent novel method of mud and new installation remains numerous investigators and the secular task of engineering technical personnel energetically.
The utility model content
The purpose of the utility model provides a kind of system of the internal heating fluidized bed sludge-drying of intermittent combustion of environmental protection and energy saving, is used for the drying of mud.
For realizing above-mentioned purpose, the utility model adopts following technical scheme.
The system of the internal heating fluidized bed sludge-drying of a kind of intermittent combustion comprises: pulsating combusting device, wet mud feed prilling granulator, internal heating fluidized bed drying machine, cleaning apparatus, odor removal; The pulsating combusting device tail pipe is connected with internal heating fluidized bed dryer entrance mouth, and internal heating fluidized bed drying machine opening for feed links to each other with wet mud feed prilling granulator; Internal heating fluidized bed dryer outlet mouth is connected with cleaning apparatus, and cleaning apparatus also is connected with odor removal; The steam-in of internal heating fluidized bed drying machine built-in heat exchanger is connected with steam (superheated vapour or saturation steam) thermal source, and the condensation-water drain of internal heating fluidized bed drying machine built-in heat exchanger is connected with boiler; Internal heating fluidized bed drying machine discharge port is connected with the siccative storehouse respectively with first step cleaning apparatus discharge port.
The internal heating fluidized bed sludge drying system of said intermittent combustion also comprises recirculation blower, and outlet, pulsating combusting device and internal heating fluidized bed dryer entrance mouth that recirculation blower connects cleaning apparatus are connected.
Said wet mud feed prilling granulator comprises sludge bin, defeated dredge pump, dredging tube, broken mud device; Mud gets into internal heating fluidized bed drying machine through sludge bin, defeated dredge pump, dredging tube, broken mud device successively.
Said pulse combustion device is a Helmholtz type pulsating combusting device, and its tail pipe is connected with fluid bed dryer.
The built-in heat exchanger of said internal heating fluidized bed drying machine, it comprises several vapor collection casees, each vapor collection case connects from beginning to end; Whole tube side is a S shape; Vapor collection case at head and the tail is respectively equipped with steam inlet and condensation-water drain, is provided with several heat transfer tubes in the adjacent vapor collection case, and each heat transfer tube two ends vertical direction is provided with tube sheet; Steam inlet connects steam source, and condensation-water drain connects boiler.
Said cleaning apparatus is a two-stage dust removal, and the first step is tornado dust collector, and the second stage is electric precipitator; Tail gas after the dedusting mixes with the pulsating combusting device tail gas stream through a recirculation blower part sends internal heating fluidized bed drying machine back to, and a part is as the secondary air retrieval system of pulsating combusting device, and another part is discharged system through odor removal.
Said odor removal is a spray column, and a waste liquid part of coming out in the spray column bottom is returned spray column, and a part gets into Sewage treatment systems.
The technology of the internal heating fluidized bed sludge-drying of a kind of intermittent combustion can directly be carried out drying with mud.Its technical process is:
(1) moisture 70%～90% mud gets into internal heating fluidized bed drying machine after granulation is pulverized;
(2) the pulsating combusting device tail gas stream is broken up mud and intensifying heat transfer, and below 50%, powder shape mud is continued heat drying by steam drying sludge to water ratio, through the control residence time of mud in bed, is dried to the moisture of requirement; The water of condensation of internal heating fluidized bed drying machine built-in heat exchanger all returns boiler and utilizes;
(3) dried mud is discharged by internal heating fluidized bed drying machine discharge port, and the dry powder of collecting with first step cleaning apparatus is delivered to the siccative storehouse;
(4) the drying moisture and the part dewatered sludge of separating out carried by the hot flue gas in the bed, behind the two-stage dust removal device, discharges system through odor removal again.
In the said step (4); Moisture that drying is separated out and part dewatered sludge are carried by the hot flue gas in the bed; Behind the two-stage dust removal device; A part is discharged system through odor removal, and a part of the mixing with the pulsating combusting device tail gas stream sent internal heating fluidized bed drying machine back to, and another part is as the secondary air retrieval system of pulsating combusting device.
In the said step (2), the required heat of said dry wet mud 30%～50% is provided by pulsating combusting device, and remaining heat is provided by steam (superheated vapour or saturation steam).
In the said step (2), said pulsating combusting device exhaust temperature is between 500～700 ℃, and ripple frequency is at 80～120Hz, and the mean air flow scope is at 15～20m/s.
In the said step (2), the pressure of said steam (superheated vapour or saturation steam) is 0.3～0.6MPa, and becomes water of condensation to return boiler after the wet mud heat exchange.
In the said step (4); Flue-gas temperature after the said dedusting is 150～200 ℃; 50～70% mix with the pulsating combusting device tail gas stream and to send internal heating fluidized bed drying machine back to, 10～20% secondary air retrieval systems as pulsating combusting device, and surplus is discharged system through odor removal.
In the said step (3), said dried mud temperature is 100～120 ℃.
The utility model adopts intermittent combustion mode dry and that internal heating fluidized bed drying combines that mud is carried out drying; The required most of heat of drying sludge is to be provided by the high built-in heat exchanger of heat exchange efficiency; Pulsating combusting device tail gas operating gas velocity is lower than conventional fluid bed dryer, and the corresponding load that reduces dust-removal system, the tail gas after the dedusting mix the oxygen level that has reduced system with the pulsating combusting device tail gas stream again; No dust combustion and explosion hazard, safe and reliable.
High-temperature tail gas stream and sound wave energy that pulsating combusting device produces with hard oscillation characteristic.Under the effect in hard oscillation flow field, the speed between Sludge Surface and flue gas, temperature and the wet thickness of concentration boundary layer that divides all reduce greatly, thereby have strengthened heat and the mass transfer process between wet mud and the air-flow; Sound wave energy can destroy the zoogloea structure; Even microbial cell wall in the destruction mud, the internal junction Heshui reduces the increase of free water component in the mud thereby cause; Accelerate sludge dehydration and dewatering efficiency; Be aided with high temperature (gas flow temperature is generally between 500～700 ℃) again, can be in the extremely short time with the powder body mud of drying sludge to water ratio below 50%, the temperature of mud generally all is no more than 50 ℃.
The steam of internal heating fluidized bed drying machine built-in heat exchanger (superheated vapour or saturation steam) thermal source provides heat to remove the residual moisture in the mud.The condensation heat transfer of steam (superheated vapour or saturation steam) improves than traditional flue gas heat exchange efficient greatly; Water of condensation all returns boiler and utilizes.
Adopt present technique to carry out drying sludge, can improve the treatment capacity of thermo-efficiency, minimizing tail gas, the oxygen level of reduction system, no dust combustion and explosion hazard, safe and reliable, can realize scale operation.
The beneficial effect of the utility model is:
(1) efficient energy-saving.The utility model adopts intermittent combustion mode dry and that internal heating fluidized bed drying combines that mud is carried out drying; Utilize the hard oscillation characteristic and the sound wave energy of the tail gas stream of intermittent combustion generation to come reinforcement sludge dry; Improved the drying efficiency of mud, and then cut down the consumption of energy; The vapour condensation heat transfer of internal heating fluidized bed drying machine built-in heat exchanger is higher than traditional hot flue gas heat exchange efficient, and the water of condensation that generates behind the steam heat-exchanging all returns boiler and utilizes; Tail gas after most of dedusting is the retrieval system UTILIZATION OF VESIDUAL HEAT IN also.
(2) tail gas and dust disposal amount are little, and environmental protection pressure is low.Dry required most of heat is to be provided by the high built-in heat exchanger of heat exchange efficiency, and pulsating combusting device tail gas operating gas velocity is lower than conventional pulsate fluidizing bed dryer, can reduce the treatment capacity of tail gas and dust effectively, and environmental protection pressure is low.
(3) security of system is reliable.The mode that adopts convection drying and contact drying to combine is carried out drying to mud, and convection drying stage flue gas oxygen content is low, the mud heat treatment time short and the mud temperature is lower, and system does not have burning and explosion hazard, and is safe and reliable.
Description of drawings
Fig. 1 is the process flow sheet of the utility model specific embodiment.
Wherein, 1. sludge bin, 2. defeated dredge pump, 3. pulsating combusting device, 4. internal heating fluidized bed drying machine, 5. tornado dust collector, 6. electric precipitator, 7. dredging tube, 8. recirculation blower, 9. spray column.
Embodiment
Below in conjunction with accompanying drawing and embodiment the utility model is described further.
Among Fig. 1, the system of the internal heating fluidized bed sludge-drying of a kind of intermittent combustion, pulsating combusting device 3 offgas duct are connected with internal heating fluidized bed drying machine 4 inlet mouths, and internal heating fluidized bed drying machine 4 links to each other respectively with tornado dust collector 5 with wet mud feed prilling granulator; Steam (superheated vapour or saturation steam) water of condensation after the steam-in of internal heating fluidized bed drying machine 4 built-in heat exchangers gets into built-in heat exchanger and wet mud heat exchange returns boiler; Internal heating fluidized bed drying machine 4 air outlets link to each other with tornado dust collector 5, electric precipitator 6 successively; Tail gas after the dedusting mixes with pulsating combusting device 3 tail gas stream through recirculation blower 8 parts sends internal heating fluidized bed drying machine 4 back to; A part is as the secondary air retrieval system of pulsating combusting device 3, and another part is through spray column 9 discharge systems.
Wet mud feed prilling granulator comprises sludge bin 1, defeated dredge pump 2, dredging tube 7, broken mud device, and sludge bin 1 is connected with defeated dredge pump 2, is connected with broken mud device through dredging tube 7, and broken mud device is installed in the internal heating fluidized bed drying machine 4 wet mud imports.
The practical implementation step of the utility model is following:
(1) moisture 70%～90% mud is delivered to the broken mud device in the wet mud import of internal heating fluidized bed drying machine by defeated dredge pump through dredging tube, and the mud after the fragmentation falls in the bed;
(2) the pulsating combusting device tail gas stream is got into internal heating fluidized bedly by internal heating fluidized bed drying machine top blast inlet, is used to break up mud and intensifying heat transfer, fast drying sludge to water ratio below 50%, and carries water vapor; Powder shape mud after predrying in internal heating fluidized bed drying machine by built-in heat exchanger in the heat that provides of steam (superheated vapour or saturation steam) continue heat drying, through the control residence time of mud in bed, be dried to the moisture of requirement; The water of condensation of internal heating fluidized bed drying machine built-in heat exchanger all returns boiler and utilizes; The required heat of said dry wet mud 30%～50% is provided by pulsating combusting device, and remaining heat is provided by steam (superheated vapour or saturation steam); Said pulsating combusting device exhaust temperature is between 500～700 ℃, and ripple frequency is at 80～120Hz, and the mean air flow scope is at 15～20m/s.The pressure of said steam (superheated vapour or saturation steam) is 0.3～0.6MPa, and becomes water of condensation to return boiler behind the wet mud of material.
(3) dried mud is discharged by internal heating fluidized bed drying machine discharge port, and the dry powder of collecting with tornado dust collector is delivered to the siccative storehouse; Dried mud temperature is 100～120 ℃.
(4) the drying moisture and the part dewatered sludge of separating out carried by the hot flue gas in the bed; Behind the two-stage dust removal device; 50～70% mix with the pulsating combusting device tail gas stream and to send internal heating fluidized bed drying machine back to; 10～20% secondary air retrieval systems as pulsating combusting device, surplus is discharged system through odor removal; Flue-gas temperature after the said dedusting is 150～200 ℃.
Though the above-mentioned accompanying drawing that combines is described the embodiment of the utility model; But be not restriction to the utility model protection domain; One of ordinary skill in the art should be understood that; On the basis of the technical scheme of the utility model, those skilled in the art need not pay various modifications that creative work can make or distortion still in the protection domain of the utility model.
Claims (7)
1. the system of the internal heating fluidized bed sludge-drying of intermittent combustion is characterized in that, comprising: pulsating combusting device, wet mud feed prilling granulator, internal heating fluidized bed drying machine, cleaning apparatus, odor removal; The pulsating combusting device tail pipe is connected with internal heating fluidized bed dryer entrance mouth, and internal heating fluidized bed drying machine opening for feed links to each other with wet mud feed prilling granulator; Internal heating fluidized bed dryer outlet mouth is connected with cleaning apparatus, and cleaning apparatus also is connected with odor removal; The steam-in of internal heating fluidized bed drying machine built-in heat exchanger is connected with steam source, and the condensation-water drain of internal heating fluidized bed drying machine built-in heat exchanger is connected with boiler; Internal heating fluidized bed drying machine discharge port is connected with the siccative storehouse respectively with first step cleaning apparatus discharge port.
2. the system of the internal heating fluidized bed sludge-drying of intermittent combustion as claimed in claim 1; It is characterized in that; The internal heating fluidized bed sludge drying system of said intermittent combustion also comprises recirculation blower, and outlet, pulsating combusting device and internal heating fluidized bed dryer entrance mouth that recirculation blower connects cleaning apparatus are connected.
3. the system of the internal heating fluidized bed sludge-drying of intermittent combustion as claimed in claim 1 is characterized in that, said wet mud feed prilling granulator comprises sludge bin, defeated dredge pump, dredging tube, broken mud device; Mud gets into internal heating fluidized bed drying machine through sludge bin, defeated dredge pump, dredging tube, broken mud device successively.
4. the system of the internal heating fluidized bed sludge-drying of intermittent combustion as claimed in claim 1 is characterized in that, the built-in heat exchanger of said internal heating fluidized bed drying machine; It comprises several vapor collection casees, and each vapor collection case connects from beginning to end, and whole tube side is a S shape; Vapor collection case at head and the tail is respectively equipped with steam inlet and condensation-water drain, is provided with several heat transfer tubes in the adjacent vapor collection case, and each heat transfer tube two ends vertical direction is provided with tube sheet; Steam inlet connects steam source, and condensation-water drain connects boiler.
5. the system of the internal heating fluidized bed sludge-drying of intermittent combustion as claimed in claim 1 is characterized in that, said pulse combustion device is a Helmholtz type pulsating combusting device, and its tail pipe is connected with fluid bed dryer.
6. the system of the internal heating fluidized bed sludge-drying of intermittent combustion as claimed in claim 1 is characterized in that, said cleaning apparatus two-stage dust removal, and the first step is tornado dust collector, the second stage is for being electric precipitator.
7. the system of the internal heating fluidized bed sludge-drying of intermittent combustion as claimed in claim 1 is characterized in that, said odor removal is a spray column, and a waste liquid part of coming out in the spray column bottom is returned spray column, and a part gets into Sewage treatment systems.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN 201220277672 CN202610084U (en) | 2012-06-13 | 2012-06-13 | Pulse combustion inner heated fluidized bed sludge-drying system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN 201220277672 CN202610084U (en) | 2012-06-13 | 2012-06-13 | Pulse combustion inner heated fluidized bed sludge-drying system |
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| CN 201220277672 Expired - Lifetime CN202610084U (en) | 2012-06-13 | 2012-06-13 | Pulse combustion inner heated fluidized bed sludge-drying system |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102690035A (en) * | 2012-06-13 | 2012-09-26 | 山东天力干燥股份有限公司 | System and process for drying sludge using pulse combustion internal heating fluid bed |
| CN103322772A (en) * | 2013-06-18 | 2013-09-25 | 华南理工大学 | Drying device of cyclonic spouted fluidized bed |
| CN106517726A (en) * | 2016-12-26 | 2017-03-22 | 南昌航空大学 | Two-stage sludge drying device and method |
| CN109011971A (en) * | 2018-08-06 | 2018-12-18 | 东华工程科技股份有限公司 | A kind of sludge drying tail gas processing equipment and method |
| CN110559680A (en) * | 2019-07-11 | 2019-12-13 | 山东省科学院能源研究所 | Device and method for vacuum flash continuous crystallization of calcium gluconate and application of device |
-
2012
- 2012-06-13 CN CN 201220277672 patent/CN202610084U/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102690035A (en) * | 2012-06-13 | 2012-09-26 | 山东天力干燥股份有限公司 | System and process for drying sludge using pulse combustion internal heating fluid bed |
| CN103322772A (en) * | 2013-06-18 | 2013-09-25 | 华南理工大学 | Drying device of cyclonic spouted fluidized bed |
| CN106517726A (en) * | 2016-12-26 | 2017-03-22 | 南昌航空大学 | Two-stage sludge drying device and method |
| CN109011971A (en) * | 2018-08-06 | 2018-12-18 | 东华工程科技股份有限公司 | A kind of sludge drying tail gas processing equipment and method |
| CN110559680A (en) * | 2019-07-11 | 2019-12-13 | 山东省科学院能源研究所 | Device and method for vacuum flash continuous crystallization of calcium gluconate and application of device |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
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| CX01 | Expiry of patent term |
Granted publication date: 20121219 |