CN104829084B - Negative pressure thermo-desorption device - Google Patents

Negative pressure thermo-desorption device Download PDF

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Publication number
CN104829084B
CN104829084B CN201510239210.0A CN201510239210A CN104829084B CN 104829084 B CN104829084 B CN 104829084B CN 201510239210 A CN201510239210 A CN 201510239210A CN 104829084 B CN104829084 B CN 104829084B
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China
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mentioned
mummification
flue gas
equipment
temperature flue
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Expired - Fee Related
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CN201510239210.0A
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Chinese (zh)
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CN104829084A (en
Inventor
周浩男
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Xi'an Hairun water world Holdings Limited
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Xi'an Hairun Water World Holdings Ltd
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Expired - Fee Related legal-status Critical Current
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Abstract

The invention discloses a negative pressure thermo-desorption device. The device is composed of a shell, wherein the shell is provided with a feed opening and a fume outlet which are formed in the top end, and a sludge outlet formed in the bottom end; at least one drying transmission mesh belt apparatus, at least one drainage partition plate, a drainage collecting apparatus, at least one high pressure flushing apparatus and at least one high temperature fume nozzle are arranged in the shell; the drying transmission mesh belt apparatus is fixedly connected with an internal bracket of the shell through a mesh belt installing frame; the drainage partition plate is fixedly connected with the mesh belt installing frame through the bracket; the high pressure flushing apparatuses are arranged at two ends of the drainage partition plate; the high temperature fume nozzles are fixedly connected with the mesh belt installing frame through a high temperature fume pipeline bracket; the drying transmission mesh belt apparatuses and a high pressure water pump are connected with an automatic control device. Afterheat of primary fume is sufficiently utilized by the device disclosed by the invention, the device is environmentally friendly, efficient and free of secondary pollution while sludge is treated, and has the energy-saving effect.

Description

Negative pressure thermal analysis apparatus
Technical field
The invention belongs to municipal sludge drying and incineration technical field, refer to a kind of negative pressure thermal analysis apparatus.
Background technology
With the quickening of the industrialized development of China and urbanization process, the raising for the treatment of rate of domestic sewage, create big Amount mud and rubbish, mud is the pollutant that a kind of property is complicated, pollutant load is high, Potential environmental risk is huge, is that height contains The solid material of the liquid of water rate, containing substantial amounts of pathogen, parasitic ovum, the heavy metal poisonous and harmful substance such as Yi Jige, hydrargyrum.Mud and Rubbish has had a strong impact on the productive life of people, causes severe contamination, municipal sludge and garbage disposal problem to environment Have become as a big the difficult problem of environmental protection of today's society urgent need to resolve.
With respect to landfill disposal and the compost treatment of mud, burning method has volume reduction, weight-loss ratio height, and processing speed is fast, no Evilization is more thorough, the advantages of reusing of energy source, is one of effective practical technique of disposing sludge.Although burning and processing sludge has Have many good qualities, but due to natural flocculation precipitation mud moisture content typically more than 90%, using mechanical dehydration device take off After water process, typically remain above 75%, so high moisture content one side can not maintain the self-holding of combustion process to carry out it is necessary to do Change and remove portion of water;On the other hand make sludge volume huge, increased transport, the difficulty of storage during burning disposal, Utilize and its inconvenient hence with the high-temperature flue gas that coal-fired power station boiler is discharged.Build sludge drying furnace to generally require very simultaneously Big one-time investment.
Current sludge anhydration burning, often directly using coal burning boiler of power station anhydration and incineration, process energy resource consumption is larger, High-temperature flue gas utilize inadequate.Mud only carries out simple process, just directly burns, purpose, single function, and its reaction difficulty comprises Following aspect:
1), in the mummification combustion process of traditional method, poisonous, harmful gass pollution environment in a large number can be discharged, affect people Ju Sheng Live;
2) traditional method single function, transport cost of disposal is high;
3) traditional method does not configure pretreatment, causes efficiency of combustion low;
4) conventional process high temperature fume afterheat wastes seriously, causes the wasting of resources.
Content of the invention
For solving above-mentioned technical problem, it is an object of the invention to provide a kind of lifting Treatment of Sludge efficiency, save energy Consume and avoid the negative pressure thermal analysis apparatus of secondary pollution.
For reaching above-mentioned purpose, a kind of negative pressure thermal analysis apparatus of the present invention, it is made up of housing, this housing is provided with: puts In charging aperture and the exhanst gas outlet of housing tip, it is placed in the sludge outlet of housing bottom;The inside of this housing is provided with: at least one Mummification transporting reticulation belt equipment, at least one water filtration separator, drainage collecting device, at least one high-pressure washing equipment and at least One high-temperature flue gas spout;Mummification transporting reticulation belt equipment is connected with enclosure interior support by guipure installation frame;Drainage Dividing plate is fixedly connected with above-mentioned guipure installation frame by support, and is welded with water pipe head at the minimum point of center edge;Filter Water collecting device connects the water pipe head on above-mentioned water filtration separator, and above-mentioned high-pressure washing equipment is located at the two ends of water filtration separator, And be connected with the high-pressure hydraulic pump that hull outside is provided with by flushing pipe;High-temperature flue gas spout passes through high-temperature flue gas support of pipelines It is fixedly connected with guipure installation frame;Above-mentioned mummification transporting reticulation belt equipment, high-pressure hydraulic pump connect automaton respectively, and by It controls respective running status.
Preferably, above-mentioned housing is circular insulation shell body.
Preferably, above-mentioned mummification transporting reticulation belt equipment is crawler type mesh belt transmission equipment.
Preferably, above-mentioned water filtration separator is rectangle, in a concave shape.
Preferably, above-mentioned drainage collecting device is pipeline, is processed filter water extraction by a pumping equipment.
Preferably, above-mentioned high-temperature flue gas spout is multiple fixed arrangement formula high-temperature flue gas spouts.
Preferably, above-mentioned high-pressure washing equipment is multiple stationary nozzles.
Beneficial effects of the present invention:
The present invention sufficiently make use of the waste heat of high-temperature flue gas, and cooperation mummification transporting reticulation belt equipment is to greatest extent to wet dirt Mud carries out drying and other treatment, while processing mud, environmental protection, high efficiency, energy saving, and non-secondary pollution.After the present invention is processed Mud will greatly reduce moisture, the character of mud also will change, can by muddy water shape liquid sludge become solid-state like mud Fragment;The anti-high-pressure washing equipment of high pressure then can be opened on demand or within the fixed cycle, cleans internal unit.
Brief description
Fig. 1 illustrates the first viewing angle constructions schematic diagram of negative pressure thermal analysis apparatus of the present invention.
Fig. 2 illustrates the second viewing angle constructions schematic diagram of negative pressure thermal analysis apparatus of the present invention.
Specific embodiment
For the ease of the understanding of those skilled in the art, the present invention is made further with accompanying drawing with reference to embodiment Bright, the content not limitation of the invention that embodiment refers to.
Shown in reference Fig. 1, Fig. 2, a kind of negative pressure thermal analysis apparatus of the present invention, it is made up of housing 1, housing 1 is circular guarantor Warm insulated enclosure, this housing 1 is provided with: is placed in charging aperture 11 and the exhanst gas outlet 12 on housing 1 top, is placed in housing 1 bottom Sludge outlet 18;The inside of this housing 1 is provided with: at least one mummification transporting reticulation belt equipment 13, at least one water filtration separator 14, One drainage collecting device 15, at least one high-pressure washing equipment 16 and at least one high-temperature flue gas spout 17;Mummification transmission network Carrying device 13 is connected with housing 1 internal stent 10 by guipure installation frame 131;Water filtration separator 14 pass through support with above-mentioned Guipure installation frame is fixedly connected, and is welded with water pipe head 141 at the minimum point of center edge;Drainage collecting device 15 connects Water pipe head 141 on above-mentioned water filtration separator 14, drainage collecting device 15 connects the pumping equipment 4 outside housing 1;Above-mentioned height Pressure flushing device 16 is located at the two ends of water filtration separator 14, and the high-pressure hydraulic pump 3 by being provided with outside flushing pipe 161 and housing 1 It is connected;It is fixing with guipure installation frame even that high-temperature flue gas spout 17 passes through high-temperature flue gas support of pipelines (in figure is not made to illustrate) Connect;Above-mentioned mummification transporting reticulation belt equipment 13, high-pressure hydraulic pump 3, pumping equipment 4, air-introduced machine 6 connects automaton 2 respectively, and It is controlled by respective running status.
In embodiment, above-mentioned mummification transporting reticulation belt equipment 13 is crawler type mesh belt transmission equipment, and guipure 134 material is not Rust steel simultaneously presses certain mesh number customization, and guipure 134 is arranged on guipure installation frame 131, mummification transporting reticulation belt equipment 13 number Amount elects three as, becomes to stagger stepped, is alternatively other numbers in other embodiment.Each mummification transporting reticulation belt equipment 13 Drivewheel 132 and driven pulley 133 are separately mounted on guipure installation frame 131, and guipure installation frame 131 support is incubated with circular The internal stent of insulated enclosure 1 is fixedly connected by bolt 7, and drivewheel 132 passes through frequency conversion motor and decelerator drives, and it is even The mode that connects is chain drive, is controlled the running status of frequency conversion motor by automaton 2.
Above-mentioned water filtration separator 14 is rectangle, and in a concave shape, overall curved surface need to smooth, and welds wherein at the minimum point at heart edge The water pipe head 141 being connected to is located at the inside of the guipure 134 of each mummification transporting reticulation belt equipment 13, separates the upper and lower of guipure 134 Surface, the support of water filtration separator 14 is directly bolted with above-mentioned guipure installation frame 131, and its position does not affect mummification and passes The reciprocating operation of defeated guipure equipment 13.
Above-mentioned drainage collecting device 15 is to be welded with pipeline, with the minimum point of above-mentioned water filtration separator 14 center edge Water pipe head 141 is threaded, by drainage collecting device 15, the water that three water filtration separators 14 collect is caused circular thermal insulation separation The outside of hot shell body 1 is processed;This drainage collecting device 15 is also connected with drawing water outside circular insulation shell body 1 and sets Standby 4.
Above-mentioned high pressure backwashing equipment 16 is multiple stationary nozzles, is connected with flushing pipe 161, flushing pipe 161 The trend that position is moved towards with above-mentioned drainage collecting device 15 is consistent, and each above-mentioned mummification transporting reticulation belt equipment 13 is furnished with two punchings Wash pipeline 161, be located at the two ends of water filtration separator 14 respectively, in relative position, each flushing pipe 161 is provided with several solid Determine shower nozzle, carry out the setting of quantity according to the actual needs, flushing pipe 161 connects outside circular insulation shell body 1 High-pressure hydraulic pump 3, provides the flushing water with pressure by high-pressure hydraulic pump 3, and high-pressure hydraulic pump 3 connects automaton 2 by line, by Automaton 2 controls its running status.
Above-mentioned high-temperature flue gas spout 17 is multiple fixed arrangement formula high-temperature flue gas spouts, and it is propped up by high-temperature flue gas pipeline Frame (in figure is not made to illustrate) and guipure installation frame 131 support are bolted, and each mummification transporting reticulation belt equipment 13 sets There is a high-temperature flue gas spout 17, be installed on the end of mummification transporting reticulation belt equipment 13 traffic direction, this high-temperature flue gas spout 17 It is connected with the air-introduced machine 6 outside circular insulation shell body 1 by high-temperature flue gas pipeline 171, high temperature cigarette is introduced by air-introduced machine 6 Gas, air-introduced machine 6 connects automaton 2 by line, controls its running status by automaton 2.
The negative pressure thermal analysis apparatus operation principle of the present invention is as follows:
First, high water content sludge is entered in negative pressure thermal analysis apparatus by charging aperture 11, after charging aperture 11 is processed, Mud is evenly distributed on the guipure 134 of mummification transporting reticulation belt equipment 13, automaton 2 passes through by certain thickness The rotating speed of line traffic control frequency conversion motor, cooperation reductor controls the rotating speed of drivewheel 132, thus controlling mummification transporting reticulation belt equipment 13 Guipure 134 gait of march, while high water content sludge is advanced on guipure, part moisture can ooze from the mesh of guipure Under filter, fall on water filtration separator 14, by drainage collecting device 15, filter water extraction is processed.
But when mud advances to end on guipure 134, due to shuttle operating structure, mud can be at guipure 134 end End falls, because three mummification transporting reticulation belt equipment 13 are stepped in staggering, therefore the mud falling can be fallen next mummification and pass On the guipure 134 of defeated guipure equipment 13, can not fall because the high-moisture percentage of mud can lead to partial sludge to be attached on guipure 134 Under, now automaton 2 controls air-introduced machine 6 to introduce high-temperature flue gas, sprays high-temperature gas by high-temperature flue gas spout 17, is inciting somebody to action The mud of attachment blow off the guipure to next mummification transporting reticulation belt equipment 13 while also play the role of a mummification to mud. High water content sludge passes through the mummification of said process and removes water, processes eventually through sludge outlet 18 natural excrement.
Wherein, high pressure backwashing equipment 16 adopts water jets under high pressure on demand or opens within the fixed cycle, within cleaning Water filtration separator 14, water jets under high pressure connects, by line, the high-pressure hydraulic pump 3 controlling by automaton 2 to be provided.
Above-mentioned high-temperature flue gas spout 17 is while persistently blowing off the mud being attached on guipure 134 additionally it is possible to be to protect Warm space make-up temperature and cleaning guipure 134 prevent guipure hole plug, and high-temperature flue gas spout 17 can enable the temperature in space It is maintained within the temperature range of requirement, meet the requirement of the mummification temperature of mud on transporting reticulation belt 134, mummification in closing space The humid flue gas that mud produces then by air-introduced machine 6 after exhanst gas outlet 12 pump-and-treat system qualified discharge it is ensured that in closing space Smoke moisture scope within requiring.Mud after being processed by said process will greatly reduce moisture, the character of mud Also will change, and solid-state like mud fragment can be become by muddy water shape liquid sludge.
Concrete application approach of the present invention is a lot, the above be only the preferred embodiment of the present invention it is noted that for For those skilled in the art, under the premise without departing from the principles of the invention, some improvement can also be made, this A little improvement also should be regarded as protection scope of the present invention.

Claims (6)

1. it is characterised in that being made up of housing, this housing is provided with a kind of negative pressure thermal analysis apparatus: is placed in entering of housing tip Material mouth and exhanst gas outlet, are placed in the sludge outlet of housing bottom;The inside of this housing is provided with: at least one mummification transporting reticulation belt sets Standby, at least one water filtration separator, drainage collecting device, at least one high-pressure washing equipment and the spray of at least one high-temperature flue gas Mouthful;Mummification transporting reticulation belt equipment is connected with enclosure interior support by guipure installation frame;Water filtration separator pass through support with Above-mentioned guipure installation frame is fixedly connected, and is welded with water pipe head at the minimum point of center edge;Drainage collecting device connects Water pipe head on above-mentioned water filtration separator, above-mentioned high-pressure washing equipment is located at the two ends of water filtration separator, and passes through flushing pipe It is connected with the high-pressure hydraulic pump that hull outside is provided with;High-temperature flue gas spout passes through high-temperature flue gas support of pipelines and guipure installation frame It is fixedly connected;Above-mentioned mummification transporting reticulation belt equipment, high-pressure hydraulic pump connect automaton respectively, and are controlled by respective fortune Row state;Above-mentioned high-temperature flue gas spout is multiple fixed arrangement formula high-temperature flue gas spouts, and it passes through high-temperature flue gas support of pipelines It is bolted with guipure installation frame support, each mummification transporting reticulation belt equipment is provided with a high-temperature flue gas spout, peace It is loaded on the end of mummification transporting reticulation belt equipment traffic direction.
2. negative pressure thermal analysis apparatus according to claim 1 are it is characterised in that above-mentioned housing is outside circular insulation Housing.
3. negative pressure thermal analysis apparatus according to claim 1 are it is characterised in that above-mentioned mummification transporting reticulation belt equipment is to carry out Belt mesh belt transmission equipment.
4. negative pressure thermal analysis apparatus according to claim 1, it is characterised in that above-mentioned water filtration separator is rectangle, become recessed Shape.
5. negative pressure thermal analysis apparatus according to claim 1 are it is characterised in that above-mentioned drainage collecting device is pipeline, By a pumping equipment, filter water extraction is processed.
6. negative pressure thermal analysis apparatus according to claim 1 are it is characterised in that above-mentioned high-pressure washing equipment is multiple solid Determine shower nozzle.
CN201510239210.0A 2015-05-12 2015-05-12 Negative pressure thermo-desorption device Expired - Fee Related CN104829084B (en)

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Application Number Priority Date Filing Date Title
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Application Number Priority Date Filing Date Title
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CN104829084B true CN104829084B (en) 2017-02-01

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116177846B (en) * 2023-05-04 2023-07-18 北京建工环境修复股份有限公司 Dewatering system of soil drip washing mud

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US3531404A (en) * 1968-04-01 1970-09-29 Union Tank Car Co Sewage treatment system
NL1001970C2 (en) * 1995-12-21 1997-06-24 Pannevis Bv Device for filtering, washing and drying a solid-liquid mixture.
CN104230138B (en) * 2014-07-11 2015-10-28 浙江三联环保机械设备有限公司 Belt-type sludge drier
CN204644097U (en) * 2015-05-12 2015-09-16 周浩男 Sub-pressure high-efficient pyrolysis device

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EXSB Decision made by sipo to initiate substantive examination
SE01 Entry into force of request for substantive examination
C41 Transfer of patent application or patent right or utility model
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Effective date of registration: 20161207

Address after: 710000 Shaanxi high tech Zone in Xi'an City Industrial Park on the eastern side of East Street Art Garden Apartment Building 1 Building 6 room 61402

Applicant after: Xi'an Hairun water world Holdings Limited

Address before: West Street in Jianye District of Nanjing City, Jiangsu province 210019 No. 198 building four unit 902 in the world in Jiangsu environmental Polytron Technologies Inc

Applicant before: Zhou Haonan

C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20170201

Termination date: 20200512

CF01 Termination of patent right due to non-payment of annual fee