CN205999262U - A kind of full anhydration system of the mud combining with biomass fuel - Google Patents

A kind of full anhydration system of the mud combining with biomass fuel Download PDF

Info

Publication number
CN205999262U
CN205999262U CN201620931959.1U CN201620931959U CN205999262U CN 205999262 U CN205999262 U CN 205999262U CN 201620931959 U CN201620931959 U CN 201620931959U CN 205999262 U CN205999262 U CN 205999262U
Authority
CN
China
Prior art keywords
mud
drying machine
biomass fuel
full
combining
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201620931959.1U
Other languages
Chinese (zh)
Inventor
邵焜琨
谢海娟
顾骏
蒋立平
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JIANGSU PHILIP ENVIRONMENTAL PROTECTION ENGINEERING Co Ltd
Original Assignee
JIANGSU PHILIP ENVIRONMENTAL PROTECTION ENGINEERING Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by JIANGSU PHILIP ENVIRONMENTAL PROTECTION ENGINEERING Co Ltd filed Critical JIANGSU PHILIP ENVIRONMENTAL PROTECTION ENGINEERING Co Ltd
Priority to CN201620931959.1U priority Critical patent/CN205999262U/en
Application granted granted Critical
Publication of CN205999262U publication Critical patent/CN205999262U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Treatment Of Sludge (AREA)

Abstract

The full anhydration system of mud that this utility model is combined with biomass fuel, including mud feeding system, sludge dry system and exhaust treatment system, mud feeding system includes the mud hopper being sequentially connected, metering conveyor and screw feeder, sludge dry system includes the primary drying machine being connected with screw feeder, the secondary drying machine being connected with primary drying machine, the biomass boiler being connected with primary drying machine, the air stove being connected with secondary drying machine, exhaust treatment system includes the cyclone separator being connected with mud hopper, the spray scrubber being connected with cyclone separator.This utility model product can send into power plant as biomass fuel, also entrance system capable of circulation carries out incineration disposal as pre-heating fuel, the mummification energy is essentially biomass fuel, low cost, facility floor space is little, high degree of automation, realize steady and continuous produce, product can adjust mud extraction moisture content according to final recycling approach, realize resources optimization and utilize.

Description

A kind of full anhydration system of the mud combining with biomass fuel
Technical field
This utility model is related to environment water-treatment technology field, and specifically a kind of mud combining with biomass fuel is complete Anhydration system.
Background technology
Municipal sewage treatment is the environmental issue that China " 15 " the Eleventh Five-Year Plan period needs that emphasis solves, and carries out dirt energetically While water process, it is faced with to its accompaniment again --- a difficult problem for specific resistance to filtration.Main in the mud of municipal sewage plant Want composition to be Organic substance, thus itself be exactly good Agricultural organic fertilizer raw material, can be comprehensively utilized, become give up into Profit.In terms of world wide, the process method of disposal of municipal sludge mainly has compost, burning, throws the various ways such as sea, landfill.Its In semi-oriented burning method technology and equipment complicated, energy consumption is big, and investment is high, and with atmosphere polluting problem;Landfill method is used The restriction on ground;Throw sea meeting Marine Pollution, marine ecosystems and human foods chain can be threatened, international convention explicit order is prohibited Only;Composting process is subject to impact of heavy metals in mud, and application has limitation;And absolutely dryization burning method have reliable and stable, can resource The advantages of change, be one of current cry highest treatment approach.
Utility model content
The purpose of this utility model is to provide that a kind of utilization rate is high, the low cost mud combining with biomass fuel is complete Anhydration system.
This utility model is achieved through the following technical solutions above-mentioned purpose:A kind of mud combining with biomass fuel is complete Anhydration system, including mud feeding system, sludge dry system and exhaust treatment system, described mud feeding system is included successively Mud hopper, metering conveyor and the screw feeder connecting, described sludge dry system is included with described screw feeder even The biomass that the secondary drying machine that the primary drying machine connecing is connected with described primary drying machine is connected with described primary drying machine The air stove that boiler is connected with described secondary drying machine, described exhaust treatment system includes the rotation being connected with described mud hopper The spray scrubber that wind separator is connected with described cyclone separator.
Further, described screw feeder adopts the method for operation of VFC.
Further, described spray scrubber inhales tower using uprightly reverse-flow washing.
Further, the fuel that described biomass boiler adopts is dewatered sludge.
Compared with prior art, the beneficial effect of the full anhydration system of mud that this utility model is combined with biomass fuel It is:
1. product can send into power plant as biomass fuel, and also entrance system capable of circulation is burned as pre-heating fuel Dispose, the mummification energy used is essentially biomass fuel, with low cost;
2. whole set process facility floor space is little, high degree of automation, easily realize steady and continuous and produce;
3. product can adjust mud extraction moisture content according to final recycling approach, realize resources optimization and utilize.
Brief description
Fig. 1 is structural representation of the present utility model.
Specific embodiment
Refer to Fig. 1, a kind of full anhydration system of the mud combining with biomass fuel, including mud feeding system, dirt Mud drying system and exhaust treatment system, mud feeding system includes mud hopper, metering conveyor and the spiral being sequentially connected Feeder, sludge dry system include two grades that the primary drying machine that is connected with screw feeder is connected with primary drying machine dry The air stove that the biomass boiler that dry machine is connected with primary drying machine is connected with secondary drying machine, exhaust treatment system include and The spray scrubber that the cyclone separator that mud hopper connects is connected with cyclone separator.
In mud feeding system, the mud in mud hopper enters metering conveyor, is then fed in screw feeder. Screw feeder, primarily to accurate measurement and add material, by the method for operation of VFC, is turned by metering screw Speed is determining dosage.
The mud of 80% moisture content is transported to primary drying machine, and steam is delivered to primary drying by biomass fuel boiler The moisture content of mud is down to 55% about from 80% after heating by machine, is that succeeding level-two mummification creates favorable conditions.Biomass boiler Using fuel be dewatered sludge.
55% water content sludge is added in secondary drying machine, will be defeated for the hot blast producing in burning process by air stove Enter secondary drying machine, be dried, 800 DEG C of drying machine input gas temperature, outlet temperature is 110 DEG C.
The dust that cyclone separator separation waste gas is taken out of, efficiency of dust collection typically 90%, the dust of collection directly with mummification dirt Mud is mixed as product.
Spray scrubber inhales tower using uprightly reverse-flow washing, has a gas-liquid separation dress on the spray system upper strata of scrubbing tower Put, this segregation apparatus is to separate absorbing liquid, block and enter blower fan system.
Washing absorption liquid circulating device is by circulating pump, nonchoking nozzle, jet pipe, cyclic water tank, solid-liquid separator, pressure gauge Deng assembly composition.The presence of the uniform of water distribution and water pollution granule is take into account during the design of washing absorption fluid circulation.Pipe Be mounted with road solid-liquid separator and using being not easily blocked, the spiral nozzle of easy accessibility.Washing absorption liquid circulating device is by electricity Control cabinet controls operation.The pump operating cycle that closes pacifies button, and circulating pump operates.The neutralizer of cyclic water tank is divided by circulating pump, solid-liquid From device, jet pipe, nonchoking nozzle, arrive cyclic water tank again it is achieved that the uninterrupted circular flow of neutralizer and oxidation solution.
Every grade of cyclic water tank of spray scrubber is equipped with moisturizing electromagnetic valve, automatic liquid level ball-cock assembly one.Moisturizing electromagnetic valve is subject to Automatic liquid level instrument control system, when liquid level is in low level, automatic liquid level instrument is opened to moisturizing solenoid signal, moisturizing electromagnetic valve, to Cyclic water tank moisturizing.When liquid level unit is in a high position, automatic liquid level instrument, to moisturizing solenoid signal, moisturizing closed electromagnetic valve, stops Only moisturizing.And have independent discharging of waste liquid system.Each system sewage draining exit, ball valve.Circulation fluid circulation one timing of cyclic water tank Between after need discharge.
Advantage of the present utility model is as follows:
1. product can send into power plant as biomass fuel, and also entrance system capable of circulation is burned as pre-heating fuel Dispose, the mummification energy used is essentially biomass fuel, with low cost;
2. whole set process facility floor space is little, high degree of automation, easily realize steady and continuous and produce;
3. product can adjust mud extraction moisture content according to final recycling approach, realize resources optimization and utilize.
Above-described is only some embodiments of the present utility model.For the person of ordinary skill of the art, On the premise of creating design without departing from this utility model, some deformation can also be made and improve, these broadly fall into this practicality New protection domain.

Claims (4)

1. a kind of full anhydration system of the mud combining with biomass fuel it is characterised in that:Including mud feeding system, mud Drying system and exhaust treatment system, described mud feeding system includes mud hopper, metering conveyor and the spiral shell being sequentially connected Rotation feeder, described sludge dry system includes the primary drying machine being connected with described screw feeder and described primary is dried The heat that the biomass boiler that the secondary drying machine that machine connects is connected with described primary drying machine is connected with described secondary drying machine Wind furnace, the cyclone separator that described exhaust treatment system includes being connected with described mud hopper is connected with described cyclone separator Spray scrubber.
2. the full anhydration system of the mud combining with biomass fuel according to claim 1 it is characterised in that:Described spiral shell Rotation feeder adopts the method for operation of VFC.
3. the full anhydration system of the mud combining with biomass fuel according to claim 1 it is characterised in that:Described spray Drench scrubbing tower and tower is inhaled using uprightly reverse-flow washing.
4. the full anhydration system of the mud combining with biomass fuel according to claim 1 it is characterised in that:Described life The fuel that material boiler adopts is dewatered sludge.
CN201620931959.1U 2016-08-25 2016-08-25 A kind of full anhydration system of the mud combining with biomass fuel Active CN205999262U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620931959.1U CN205999262U (en) 2016-08-25 2016-08-25 A kind of full anhydration system of the mud combining with biomass fuel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620931959.1U CN205999262U (en) 2016-08-25 2016-08-25 A kind of full anhydration system of the mud combining with biomass fuel

Publications (1)

Publication Number Publication Date
CN205999262U true CN205999262U (en) 2017-03-08

Family

ID=58196899

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620931959.1U Active CN205999262U (en) 2016-08-25 2016-08-25 A kind of full anhydration system of the mud combining with biomass fuel

Country Status (1)

Country Link
CN (1) CN205999262U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106145599A (en) * 2016-08-25 2016-11-23 江苏菲力环保工程有限公司 A kind of full anhydration system of the mud combined with biomass fuel

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106145599A (en) * 2016-08-25 2016-11-23 江苏菲力环保工程有限公司 A kind of full anhydration system of the mud combined with biomass fuel

Similar Documents

Publication Publication Date Title
CN102816575B (en) The device of biomass destructive distillation cracking process and process
CN104628237B (en) Sludge drying incineration system based on thermal power plant
CN105536436A (en) Organic waste gas purification device and purification method aiming at asphalt processing production
CN204338559U (en) Municipal refuse and mud total system
CN108105790A (en) Oily sludge glows processing unit
CN102351396B (en) Sludge drying equipment using waste heat of landfill gas power generation
CN108326012A (en) The cooperation-gasified method of multi-element material and its system
CN201310895Y (en) Municipal domestic refuse drying pretreatment device
CN205443212U (en) Garbage pyrolytic gasification flue gas processing system
CN206256023U (en) A kind of domestic garbage treating system based on microwave cracking
CN205999262U (en) A kind of full anhydration system of the mud combining with biomass fuel
CN204138601U (en) A kind of pyrolyzing sludge gasification treatment system
CN103449700A (en) Sludge quick-dry continuous heat-supplying wind-dry type drying device
CN103712216B (en) Mud and rubbish combine incineration thermoelectric treatment system and processing method
CN206244619U (en) A kind of sludge treating system based on hydrothermal carbonization
CN203768193U (en) Vitrified sludge disposal system
CN204529636U (en) A kind of sludge drying and incineration system relying on heat power plant
CN101974351B (en) Scale fixed bed biomass gasification power generation production technology and suite of equipment
CN208265796U (en) Drying coupling apparatus is concentrated in landfill leachate
CN105985792B (en) A kind of rubbish destructive distillation at charcoal method
CN202968336U (en) Multilayer running hot air drying device
CN108405549B (en) Method and device for preventing and treating scaling blockage of refuse landfill by utilizing furnace slag and landfill gas
CN207313414U (en) Utilize the sludge anhydration burning device of solar energy
CN113072283A (en) Biochemical sludge treatment system and treatment process thereof
CN105481037A (en) Substance thermal decomposition and sub-treatment device

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant