CN104344689B - A kind of method of Hot-blast Heating house refuse transpiring moisture and drying unit thereof - Google Patents

A kind of method of Hot-blast Heating house refuse transpiring moisture and drying unit thereof Download PDF

Info

Publication number
CN104344689B
CN104344689B CN201410548253.2A CN201410548253A CN104344689B CN 104344689 B CN104344689 B CN 104344689B CN 201410548253 A CN201410548253 A CN 201410548253A CN 104344689 B CN104344689 B CN 104344689B
Authority
CN
China
Prior art keywords
rotary kiln
house refuse
rubbish
soft seal
wind mechanism
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.)
Expired - Fee Related
Application number
CN201410548253.2A
Other languages
Chinese (zh)
Other versions
CN104344689A (en
Inventor
史金麟
殷梅芳
史惠元
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.)
Shi Huiyuan
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN201410548253.2A priority Critical patent/CN104344689B/en
Publication of CN104344689A publication Critical patent/CN104344689A/en
Application granted granted Critical
Publication of CN104344689B publication Critical patent/CN104344689B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The present invention relates to house refuse drying and processing field, method and drying unit thereof particularly to a kind of Hot-blast Heating house refuse transpiring moisture, the method is persistently to heat to house refuse, makes the temperature of house refuse be maintained between 100 DEG C 270 DEG C, to evaporate moisture therein;Drying unit, including rotary kiln, the length direction of described rotary kiln is provided with heater.The method is persistently to heat to house refuse, evaporates moisture therein, and the garbage energy obtaining drying is enough in gasification and makes combustion gas, solves and the rubbish do not dried is put into the problem that gasifier system combustion gas can not remain properly functioning.This drying unit both make use of the continuous rolling of rotary kiln, and it is the most homogeneous that house refuse can be dried after putting into;On the other hand the length direction along rotary kiln with the addition of heater, makes whole rotary kiln be in the state being persistently heated, and rubbish is constantly heated to evaporate the moisture contained in rubbish in rolling, makes rubbish progressively be dried.

Description

A kind of method of Hot-blast Heating house refuse transpiring moisture and drying dress thereof Put
Technical field
The present invention relates to house refuse drying and processing field, in particular to a kind of hot blast The method of heating house refuse transpiring moisture and drying unit thereof.
Background technology
Rubbish aqueous about 50%, calorific value presses 1000kcal/kg, takes equivalent proportion 0.15, i.e. Gas-air amount is theoretical air requirement 15% sent into, namely rubbish institute carbon containing (C) About the 15% of total amount burns at burner hearth naked light, produces CO2Gas heat release, for sequential reduction district Thering is provided heat, about the 85% of rubbish institute carbon containing (C) total amount becomes carbide semicoke (as black The grain of rice, is commonly called as semicoke), flow to reducing zone and CO with the revolution of rotary kiln2Gas reaction is raw Become combustion gas.It follows that it is 1000kcal/kg × 15%=150 that rubbish discharges heat in stove Kcal/kg, and aqueous about 50% i.e. 0.5kg, its water evaporation calorific requirement be 600kcal/kg × 0.5kg=300kcal.Water evaporation power consumption 300kcal > rubbish release heat 150kcal, therefore, Directly the rubbish do not dried is put into gasifier system combustion gas, it is impossible to maintain and run.
Application No. 200810229585.9 discloses domestic waste and is dried pretreatment side Method and device, use single drying machine to be dried rubbish, but so increase in this application Having added the cost of operation, and treating capacity is little, energy consumption is big.
Application No. 200910075330.6 discloses and utilizes rubbish gas heating directly also The method of reducing gases in former ferrum, with the addition of lump coal, moulded coal or coke during burning away the refuse To increase the heat of burning, but so produce too many CO2Waste gas, is applied to combustion gas processed meaning And gasify unsuccessfully.In like manner, when using the mode sending combustion air, gasification furnace maintains and runs more, Also too many CO can be produced2Waste gas.
1 gasification furnace can be with gasification process house refuse 1000t/d, and wherein moisture is about 500t, If the combustion gas containing water vapor 500t/d that gasification furnace is discharged, it is clear that cannot be properly functioning.Therefore, Rubbish cannot be dried in gasification furnace.
At present, domestic and international rubbish is dried and is mainly used two ways, the drying heat of a kind of employing Source > 270 DEG C, but, plastics can dissolve 270 DEG C of temperatures above, rubbish can the group of being formed, Occluding device makes drying failure;The another kind of drying thermal source < 270 DEG C used, room temperature humidity Rubbish send into dehydrator, the thermal source of dehydrator can be made to be rapidly decreased to less than 100 DEG C, moisture without Method is evaporated, and dries unsuccessfully.Exactly because there is no garbage drier the most both at home and abroad, thus raw Rubbish combustion gas of living tries to suffer defeat after defeat repeatly.
In view of this, the special proposition present invention.
Summary of the invention
The first object of the present invention is to provide a kind of Hot-blast Heating house refuse transpiring moisture Method, persistently gives heat, makes the temperature of house refuse be maintained at 100 DEG C-270 DEG C house refuse Between, to evaporate moisture therein, obtain the rubbish dried, be subsequently used for gasification and make Combustion gas, to solve at present the rubbish do not dried to be put into gasifier system combustion gas, it is impossible to just maintaining The problem often run.
The second object of the present invention is to provide a kind of drying unit, and this device is at rotary kiln On the basis of improve further, both make use of the continuous rolling of rotary kiln, so that raw It is the most homogeneous that rubbish alive can be dried after putting into;On the other hand along the length direction of rotary kiln With the addition of heater, make whole rotary kiln be in the state being persistently heated so that it is interior rubbish Rubbish is constantly heated to evaporate the moisture contained in rubbish in rolling, make rubbish progressively by It is dried.
In order to realize the above-mentioned purpose of the present invention, spy by the following technical solutions:
A kind of method of Hot-blast Heating house refuse transpiring moisture, comprises the following steps:
House refuse is persistently given heat, makes the temperature of house refuse be maintained at 100 DEG C-270 DEG C Between, to evaporate moisture therein.
The method of a kind of Hot-blast Heating house refuse transpiring moisture that the present invention provides, to life Heat persistently given by rubbish, as heated house refuse in rotary kiln, arranges many along rotary kiln length Individual heater, makes rubbish heated at different parts all energy of rotary kiln, so that raw Rubbish of living can be dried moving to rotary kiln afterbody when.So make the temperature of house refuse Degree can be maintained at more than 100 DEG C, to evaporate moisture therein, obtains the rubbish dried, Then the garbage energy dried is enough in gasification and makes combustion gas, solves the rubbish will do not dried at present Rubbish puts into gasifier system combustion gas, it is impossible to maintain properly functioning problem.
Preferably, percentage, the water content of the rubbish of described drying be 10% with Under.The rubbish so dried can preferably be used for gasification and make combustion gas, at present will solve Gasifier system combustion gas put into by the rubbish do not dried, it is impossible to maintain properly functioning problem.
Preferably, persistently produce to the gasification furnace that hot thermal source is combustion gas processed for house refuse Slag be raw material.As: in rotary kiln, heat house refuse, the heater of rotary kiln Be with gasifier system combustion gas produce slag as raw material, heater can be air stove etc.. Preferably, described house refuse is constantly rolled in heating process.House refuse is hankered adding The constantly uniform heating of rolling, the most beneficially rubbish, the most beneficially moisture in rubbish is constantly steamed Issue.
Present invention also offers the baking of the method implementing Hot-blast Heating house refuse transpiring moisture Equipment for drying, including rotary kiln, the length direction of described rotary kiln is provided with heater.
The drying unit that the present invention provides is to change further on the basis of rotary kiln Enter, both make use of the continuous rolling of rotary kiln, so that what house refuse can be dried after putting into The most homogeneous;On the other hand the length direction along rotary kiln with the addition of heater, makes whole Rotary kiln is in the state being persistently heated so that it is interior rubbish is constantly heated in rolling Evaporate the moisture contained in rubbish, make rubbish progressively be dried.
Preferably, described heater include thermal source and be enclosed on described rotary kiln soft close Envelope is by wind mechanism, and described thermal source is connected by pipeline by wind mechanism with described soft seal;
Described soft seal is included thermal insulation layer and soft close with described rotary kiln linear contact lay by wind mechanism Sealing, described soft seal is had space by between wind mechanism and described rotary kiln, is used for being passed through institute State the steam that thermal source provides.
Thermal source provides heat, it is provided that heat be transported to soft seal by wind mechanism through pipeline, soft Seal and be could be arranged to be wrapped circumferentially around along rotary kiln by wind mechanism, or part covers rotary kiln; Rotary kiln rotates, and soft seal is not rotated with the rotation of rotary kiln by wind mechanism, and soft seal is subject to Wind mechanism is fixed by support, and soft seal is linear contact lay by wind mechanism and rotary kiln, at high temperature Under can seal gas, soft seal, by there being space between wind mechanism and rotary kiln, is used for being passed through The steam that thermal source provides.
Wherein, thermal source can be the equipment such as air stove, heat exchanger, it is also possible to for the heat reclaimed Amount, the steam etc. produced such as the gasification furnace for burning away the refuse;It can also be several device one Rise and use.Preferably, the thermal source of heater includes air stove.If selection air stove, The slag that air stove produces with the gasification furnace of combustion gas processed is as raw material;Additionally, what air stove was discharged Flue gas is less than 260 DEG C, is transported to the burner hearth of rotary kiln, and flue dust therein becomes the one of rubbish Part, together with the steam that waste gas evaporates with rubbish, through pipeline flow-direction cooler.So Both reclaim the heat of air stove, dispense again its flue gas produced of individual processing.If it is hot The heat that wind furnace produces can not meet needs, it is also possible to adds heat exchanger or other heating Device is given simultaneously and is carried heat by wind mechanism.
At 1 atmosphere pressure the water 1kg of 20 DEG C is heated as steam, needs hectic fever Can 594.53kcal (heat of vaporization of 1kg water);1kg water is heated to 100 DEG C, often heats increase 1 DEG C of heat energy 1kcal to be consumed (this is 1kg specific heat of water).1t rubbish water content is according to 50% Calculating, dry to moisture content 10%, specific heat to calculate according to heating 500kg water, and vaporizes Heat calculates according to 400kg water.Rubbish mean temperature is according to 20 DEG C of calculating.Then: dry 1t Rubbish need consume heat energy: (80kcal/kg × 500kg+594.53kcal/kg × 400kg) ÷ 7000kcal/kg mark coal=40kg marks coal.The present invention does thermal source without coal, but burns gasification The slag that fire grate goes out provides thermal source as raw material.
The burning of gasifier system combustion gas is different from the phosphorus content of the slag that naked light burns, and naked light fires Burning belongs to oxygen-enriched abundant burning, belongs to oxidizing atmosphere, and C+O occurs in stove2=CO2, naked light The phosphorus content of the slag after burning is the least, about 3-5%;Gasification furnace wants output combustion gas, stove Interior needs are carried out under reducing atmosphere, and carbon (C) cannot be with oxygen (O2) reaction, carbon Namely can only carry out under the atmosphere of anoxia with carbon dioxide reaction, the reaction of generation is C+CO2=2CO, belongs to reduction reaction, and this reaction exists saturation problem, namely exists Boiler slag carbon content 24%, combustion gas are containing CO2Also it is when 24%, to reach balance (no longer reaction), Therefore, the boiler slag carbon content discharged from gasification furnace is 24%.The slag that gasification furnace is discharged is used for Combustion of Hot Air Furnace, the heat of generation is converted to hot-air seasoning rubbish, comprehensively make use of residual The energy, make drying rubbish and combustion gas processed form complete supply chain, this supply chain more ring Protect.
As: in order to preferably prevent distributing of heat in steam, soft seal is permissible by wind mechanism It is set to four layers, as in figure 2 it is shown, be followed successively by the first heat-resisting steel layer 8, wear-resisting from top to bottom Stratum reticulare 9, soft composite layer 10 and the second heat-resisting steel layer 11, wherein, soft composite layer Use the soft material of high abrasion, such as: high wear-resistant rubber, high abrasion TPV material etc., soft Composite layer and rotary kiln linear contact lay.The soft seal of this structure is prone to fixing by wind mechanism, And it is durable.
Preferably, rotary kiln is horizontal installation, and the gradient of installation is 2-6%.So install After, rubbish is put into the kiln hood of rotary kiln, with the revolution of rotary kiln, rubbish from kiln hood to kiln Tail moves, and rubbish also constantly rolls with the rotation of rotary kiln, and rubbish moves at past kiln tail During be constantly heated, as being heated to 40 DEG C by kiln hood, during moving toward kiln tail Progressively it is heated to 60 DEG C, 80 DEG C, 100 DEG C, 120 DEG C etc., thus is constantly dried, pass through Adjusting the temperature of the heater of rotary kiln, when making rubbish arrive kiln tail, rubbish is oven-dried.
Empirical tests, a length of 6-45m of the rotary kiln of use, a diameter of 1-5 of rotary kiln M, the length direction at rotary kiln arranges a heater, the temperature of steam every 3-4m Degree is not more than 270 DEG C, can well realize being oven-dried when rubbish arrives kiln tail, and temperature Being not more than 270 DEG C, the plastics in heated rubbish will not be agglomerating, thus does not results in stifled The phenomenon of plug equipment.Preferably, a length of 6-45m of described rotary kiln, described rotary kiln A diameter of 1-5m, the length direction of described rotary kiln arranges one every 3-4m and adds hot charging Putting, the temperature of described steam is not more than 270 DEG C.
Length according to rotary kiln and diameter, adjust different hot air temperature so that rubbish It is oven-dried.Further, the temperature of described steam is 150-270 DEG C.
Preferably, described thermal source and described soft seal are provided with air-introduced machine by between wind mechanism, The rotary kiln position that described soft seal layer covers is provided with multiple through hole.Air-introduced machine is by hot blast not Disconnected it is incorporated into soft seal by between wind mechanism and rotary kiln, rotary kiln arranges multiple through hole, So that hot blast is constantly blown in rotary kiln, make the rubbish in rotary kiln in constantly rolling Air-blowing of being heated is moved, and significantly accelerates the rate of drying of rubbish.
Preferably, being provided with raising material unit in described rotary kiln, described raising material unit is for along institute State rotary kiln inwall and be provided with multiple lifting bucket.Rubbish rolls with the rotation of rotary kiln, raises The rubbish of rotary kiln is preferably disperseed by material device, and rubbish is constantly mentioned by lifting bucket Raising again, soft seal is steamed by the hot blast step step by step that wind mechanism the is sent into water outlet that evaporates by heat Gas, rubbish is dried faster.
Cooler that preferably, described drying unit also includes being sequentially connected with by pipeline, Gas-liquid separator and foul smell decomposition box.
Steam and the waste gas of rotary kiln evaporation are first passed through cooler, after cooling by pipeline Steam and waste gas are passed through gas-liquid separator, and gas-liquid separator separates goes out gas and liquid, liquid Getting final product qualified discharge through simple process, isolated gas contains frowziness, and foul smell includes: ammonia (NH3), trimethylamine (C3H9N), hydrogen sulfide (H2S), methanthiol (CH4S), first sulfur Ether (C2H6S), in addition to the boiling point 37.3 DEG C of methyl sulfide, remaining the highest 7.6 DEG C of just boiling, They evaporate with steam, obtain through gas-liquid separator separates after cooled device again, separate The gas gone out pumps into foul smell decomposition box, and stink is converted into the nutrient substance of biological bacteria, stink zero Discharge.Without the discharge of garbage leachate in whole processing procedure.
During Gai, foul smell decomposition box uses the commercially available foul smell decomposition box removing stink, Can use deodorizer, or biological bacteria decomposition box, or vegetation water deodorization etc., such as: buy The biological bacteria decomposition box of gloomy source great achievement waste odour-gas cleaning equipment Manufacturing Co., Ltd from Yangzhou, 25 Second can vent gas up to standard.
Compared with prior art, the invention have the benefit that
(1) by give house refuse persistently give heat by the way of, make house refuse continuous Heated, the moisture that rubbish contains constantly is evaporated, and rubbish is oven-dried, very well Solve existing because rubbish can not dry or asking because of the too high occluding device of temperature Topic;
(2) rotary kiln is horizontal installation, and the gradient of installation is 2-6%, is put into back by rubbish The kiln hood of rotary kiln, with the revolution of rotary kiln, rubbish moves to kiln tail from kiln hood, rubbish also with The rotation of rotary kiln and constantly roll, rubbish is constantly heated during moving toward kiln tail, Evaporate moisture therein, thus constantly dried, by adjusting the heater of rotary kiln Temperature, make rubbish arrive kiln tail time, rubbish is oven-dried;
(3) on rotary kiln, interpolation soft seal, by wind mechanism, is well collected heat, is made Rotary kiln is in rotation process, and rubbish is constantly heated, and soft seal is covered by wind mechanism Rotary kiln on be provided with multiple through hole so that hot blast is constantly blown in rotary kiln, make The air-blowing of being heated in constantly rolling of rubbish in rotary kiln is moved, and significantly accelerates the dry of rubbish Dry speed;
(4) being provided with raising material unit in rotary kiln, rubbish turns in the rotation with rotary kiln Preferably disperseed by raising material unit during rolling, further speeded up the drying rate of rubbish;
(5) drying unit also includes cooler, the gas-liquid separation being sequentially connected with by pipeline Device and foul smell decomposition box, without garbage leachate and the discharge of pollutant in whole processing procedure;
(6) thermal source of heater includes air stove, and air stove is with the gasification of combustion gas processed The slag that stove produces is raw material, and the slag that well make use of combustion gas processed to produce makes baking Dry rubbish and combustion gas processed form complete supply chain, the more environmental protection of this supply chain.
Accompanying drawing explanation
In order to be illustrated more clearly that the specific embodiment of the invention or technical side of the prior art Case, will make the accompanying drawing used required in detailed description of the invention or description of the prior art below Introduce simply, it should be apparent that, the accompanying drawing in describing below is some enforcements of the present invention Mode, for those of ordinary skill in the art, in the premise not paying creative work Under, it is also possible to other accompanying drawing is obtained according to these accompanying drawings.
The side of the Hot-blast Heating house refuse transpiring moisture that Fig. 1 provides for the embodiment of the present invention 1 The schematic diagram of the drying unit of method;
The soft seal that Fig. 2 provides for the present invention is by the generalized section of wind mechanism.
Reference: 1, kiln hood;2, soft seal is by wind mechanism;3, support;4, hot blast Stove;5, cooler;6, gas-liquid separator;7, biological bacteria decomposition box;8, first is heat-resisting Steel layer;9, wear-resisting stratum reticulare;10, soft composite layer;11, the second heat-resisting steel layer.
Detailed description of the invention
Below in conjunction with embodiment, embodiment of the present invention are described in detail, but this Skilled person is it will be appreciated that the following example is merely to illustrate the present invention, and should not regard For limiting the scope of the present invention.Unreceipted actual conditions person in embodiment, according to normal condition Or the condition of manufacturer's suggestion is carried out.Instrument unreceipted production firm person, is permissible Conventional products by commercially available acquisition.
Embodiment 1
As it is shown in figure 1, the horizontal rotary kiln that installs back, the gradient of installation is 2%, the revolution of selection The a length of 6m of kiln, a diameter of 1m, the length direction of rotary kiln arranges one every 3m Individual heater;
Heater includes air stove 4 with the soft seal being enclosed on described rotary kiln by blower fan Structure 2, soft seal is included thermal insulation layer and the soft seal layer with rotary kiln linear contact lay by wind mechanism 2, Soft seal is wrapped circumferentially around along rotary kiln by wind mechanism 2, and and rotary kiln between leave space, Support 3 is used for fixing soft seal and is produced with the gasification furnace of combustion gas processed by wind mechanism 2, air stove 4 Raw slag is raw material, it is provided that steam be passed through soft seal by blower fan through air-introduced machine by pipeline Structure 2, the rotary kiln position that soft seal is covered by wind mechanism 2 is provided with multiple through hole, hot blast It is blown in rotary kiln, wherein, temperature 250-270 DEG C of steam, the flue gas that air stove produces Being passed through in rotary kiln by pipeline, rotary kiln inwall is provided with multiple lifting bucket;
House refuse after broken sorting is transported to kiln hood 1 and is sent into by drawing-in devices such as conveyers In rotary kiln, with the revolution of rotary kiln, rubbish moves to kiln tail from kiln hood, rotary kiln inwall Rubbish is mentioned and raises by multiple lifting buckets of upper setting, is sent into by wind mechanism 2 by soft seal Hot blast step step by step evaporate by heat out steam, rubbish is oven-dried;
Steam and the waste gas of rotary kiln evaporation are first passed through cooler 5, after cooling by pipeline Steam and waste gas be passed through gas-liquid separator 6, gas-liquid separator 6 isolates gas and liquid, Liquid gets final product qualified discharge through simple process, and isolated gas pumps into buys from Yangzhou gloomy source The biological bacteria decomposition box 7 of great achievement waste odour-gas cleaning equipment Manufacturing Co., Ltd, stink is converted into The nutrient substance of biological bacteria, gets final product vent gas up to standard, stink zero-emission in 25 seconds;
Without the discharge of garbage leachate in whole processing procedure, the rubbish of drying can be directly used for Preparation combustion gas.
Embodiment 2
The horizontal rotary kiln that installs back, the gradient of installation is 4%, the rotary kiln of selection a length of 20m, a diameter of 5m, the length direction of rotary kiln arranges a heater every 4m;
Heater includes air stove, heat exchanger and the soft seal wind-engaging being wrapped on rotary kiln Mechanism, soft seal is included thermal insulation layer and the soft seal layer with rotary kiln linear contact lay by wind mechanism, Soft seal layer is wrapped circumferentially around along rotary kiln, and and rotary kiln between leave space, air stove with The slag that the gasification furnace of combustion gas processed produces is raw material, the steam warp that air stove and heat exchanger produce Air-introduced machine is passed through soft seal by wind mechanism, the revolution that soft seal is covered by wind mechanism by pipeline Kiln position is provided with multiple through hole, and hot blast is blown in rotary kiln, and wherein, the temperature of steam is 200-250 DEG C, the flue gas that air stove produces is passed through in rotary kiln by pipeline, rotary kiln inwall It is provided with multiple lifting bucket;
House refuse after broken sorting is transported to kiln hood and is sent into back by drawing-in devices such as conveyers In rotary kiln, with the revolution of rotary kiln, rubbish moves to kiln tail from kiln hood, on rotary kiln inwall Rubbish is mentioned and raises by the multiple lifting buckets arranged, the heat sent into by wind mechanism by soft seal Wind step step by step evaporates by heat out steam, and rubbish is oven-dried;
Steam and the waste gas of rotary kiln evaporation are first passed through cooler, after cooling by pipeline Steam and waste gas are passed through gas-liquid separator, and gas-liquid separator separates goes out gas and liquid, liquid Getting final product qualified discharge through simple process, isolated gas pumps into buys from Yangzhou gloomy source great achievement The biological bacteria decomposition box of waste odour-gas cleaning equipment Manufacturing Co., Ltd, stink is converted into biological bacteria Nutrient substance, 25 seconds can vent gas up to standard, stink zero-emission;
Without the discharge of garbage leachate in whole processing procedure, the rubbish of drying can be directly used for Preparation combustion gas.
Embodiment 3
The horizontal rotary kiln that installs back, the gradient of installation is 6%, the rotary kiln of selection a length of 45m, a diameter of 3m, the length direction of rotary kiln arranges a heater every 3m;
Heater includes that air stove and the soft seal that is enclosed on described rotary kiln are by blower fan Structure, soft seal is included thermal insulation layer and the soft seal layer with rotary kiln linear contact lay by wind mechanism, soft Sealant is wrapped circumferentially around along rotary kiln, and and rotary kiln between leave space, air stove with system The slag that the gasification furnace of combustion gas produces is raw material, it is provided that steam led to by pipeline through air-introduced machine Entering soft seal by wind mechanism, the rotary kiln position that soft seal is covered by wind mechanism is provided with multiple Through hole, hot blast is blown in rotary kiln, wherein, and temperature 150-200 DEG C of steam, air stove The flue gas produced is passed through in rotary kiln by pipeline, and rotary kiln inwall is provided with multiple lifting bucket;
House refuse after broken sorting is transported to kiln hood and is sent into back by drawing-in devices such as conveyers In rotary kiln, with the revolution of rotary kiln, rubbish moves to kiln tail from kiln hood, on rotary kiln inwall Rubbish is mentioned and raises by the multiple lifting buckets arranged, the heat sent into by wind mechanism by soft seal Wind step step by step evaporates by heat out steam, and rubbish is oven-dried;
Steam and the waste gas of rotary kiln evaporation are first passed through cooler, after cooling by pipeline Steam and waste gas are passed through gas-liquid separator, and gas-liquid separator separates goes out gas and liquid, liquid Getting final product qualified discharge through simple process, isolated gas pumps into buys from Yangzhou gloomy source great achievement The biological bacteria decomposition box of waste odour-gas cleaning equipment Manufacturing Co., Ltd, stink is converted into biological bacteria Nutrient substance, 25 seconds can vent gas up to standard, stink zero-emission;
Without the discharge of garbage leachate in whole processing procedure, the rubbish of drying can be directly used for Preparation combustion gas.
The method of the Hot-blast Heating house refuse transpiring moisture that above example provides is by giving House refuse persistently gives the mode of heat, makes house refuse constantly be heated, the water that rubbish contains Dividing and be constantly evaporated, rubbish is oven-dried, and well solves existing because rubbish can not Dry or because of the problem of the too high occluding device of temperature.Concrete drying unit include rotary kiln, Heater, cooler, gas-liquid separator and foul smell decomposition box.By horizontal for rotary kiln installation, The gradient installed is 2-6%, and rubbish is put into the kiln hood of rotary kiln, with the revolution of rotary kiln, Rubbish moves to kiln tail from kiln hood, and rubbish also constantly rolls with the rotation of rotary kiln, rubbish Constantly heated by heater during moving toward kiln tail, evaporate moisture therein, Thus constantly dried, by adjusting the temperature of the heater of rotary kiln, make rubbish arrive During kiln tail, rubbish is oven-dried.Wherein, rotary kiln adds soft seal by wind mechanism, energy Enough well collecting heat, make rotary kiln in rotation process, rubbish is constantly heated, and And it is provided with multiple through hole, so that hot blast is not on the rotary kiln that covered by wind mechanism of soft seal Disconnected it is blown in rotary kiln, makes the air-blowing of being heated in constantly rolling of the rubbish in rotary kiln move, Significantly accelerate the rate of drying of rubbish;Additionally, be provided with raising material unit in rotary kiln, Rubbish is preferably disperseed by raising material unit when rolling in the rotation with rotary kiln, enters one Step accelerates the drying rate of rubbish.The drying unit that the present invention provides is in whole processing procedure Middle without garbage leachate with the discharge of pollutant, safety non-pollution.
Although illustrate and describing the present invention with specific embodiment, but it will be appreciated that May be made that without departing from the spirit and scope of the present invention many other change and Amendment.It is, therefore, intended that include in the following claims belonging in the scope of the invention All such changes and modifications.

Claims (4)

1. the method for a Hot-blast Heating house refuse transpiring moisture, it is characterised in that bag Include following steps:
To house refuse persistently give heat, make the temperature of house refuse be maintained at 100 DEG C-270 DEG C it Between, to evaporate moisture therein;
Percentage, the water content of the rubbish of drying is less than 10%;
The slag persistently produced to the gasification furnace that hot thermal source is combustion gas processed for house refuse is Raw material;
The method of described Hot-blast Heating house refuse transpiring moisture is carried out by drying unit, described Drying unit includes that rotary kiln, the length direction of described rotary kiln are provided with heater;
Rotary kiln is horizontal installation, and the gradient of installation is 2-6%;
The a length of 6-45m of described rotary kiln, a diameter of 1-5m of described rotary kiln, described The length direction of rotary kiln arranges a heater every 3-4m, and the temperature of steam is 150-270℃;
Described heater includes thermal source with the soft seal being enclosed on described rotary kiln by blower fan Structure, described thermal source is connected by pipeline by wind mechanism with described soft seal;
Described soft seal is included thermal insulation layer and soft close with described rotary kiln linear contact lay by wind mechanism Sealing, described soft seal is had space by between wind mechanism and described rotary kiln, is used for being passed through described The steam that thermal source provides;
Described thermal source and described soft seal by being provided with air-introduced machine between wind mechanism, described soft seal The rotary kiln position that layer covers is provided with multiple through hole;
Cooler that described drying unit also includes being sequentially connected with by pipeline, gas-liquid separator and Foul smell decomposition box.
The method of Hot-blast Heating house refuse transpiring moisture the most according to claim 1, It is characterized in that, described house refuse is constantly rolled in heating process.
3. one kind is steamed according to the Hot-blast Heating house refuse described in any one of claim 1-2 The drying unit of the method flooded point, it is characterised in that include rotary kiln, described rotary kiln Length direction is provided with heater;
Rotary kiln is horizontal installation, and the gradient of installation is 2-6%;
The a length of 6-45m of described rotary kiln, a diameter of 1-5m of described rotary kiln, described The length direction of rotary kiln arranges a heater every 3-4m, and the temperature of described steam is 150-270℃;
Described heater includes thermal source with the soft seal being enclosed on described rotary kiln by blower fan Structure, described thermal source is connected by pipeline by wind mechanism with described soft seal;
Described soft seal is included thermal insulation layer and soft close with described rotary kiln linear contact lay by wind mechanism Sealing, described soft seal is had space by between wind mechanism and described rotary kiln, is used for being passed through described The steam that thermal source provides;
Described thermal source and described soft seal by being provided with air-introduced machine between wind mechanism, described soft seal The rotary kiln position that layer covers is provided with multiple through hole;
Cooler that described drying unit also includes being sequentially connected with by pipeline, gas-liquid separator and Foul smell decomposition box.
Drying unit the most according to claim 3, it is characterised in that described revolution Being provided with raising material unit in kiln, described raising material unit is for be provided with multiple along described rotary kiln inwall Lifting bucket.
CN201410548253.2A 2014-10-16 2014-10-16 A kind of method of Hot-blast Heating house refuse transpiring moisture and drying unit thereof Expired - Fee Related CN104344689B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410548253.2A CN104344689B (en) 2014-10-16 2014-10-16 A kind of method of Hot-blast Heating house refuse transpiring moisture and drying unit thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410548253.2A CN104344689B (en) 2014-10-16 2014-10-16 A kind of method of Hot-blast Heating house refuse transpiring moisture and drying unit thereof

Publications (2)

Publication Number Publication Date
CN104344689A CN104344689A (en) 2015-02-11
CN104344689B true CN104344689B (en) 2016-08-24

Family

ID=52500810

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410548253.2A Expired - Fee Related CN104344689B (en) 2014-10-16 2014-10-16 A kind of method of Hot-blast Heating house refuse transpiring moisture and drying unit thereof

Country Status (1)

Country Link
CN (1) CN104344689B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111043867B (en) * 2019-10-28 2021-09-14 鞍钢股份有限公司 System and method for treating household garbage by utilizing ironmaking waste heat

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1133965A (en) * 1995-04-11 1996-10-23 拜尔公司 Device for supplying gas to rotary kilns
CN101050859A (en) * 2007-04-17 2007-10-10 史金麟 Method for gasifying and burning domestic garbage
CN201032153Y (en) * 2007-02-07 2008-03-05 史金麟 Honeycomb grate incinerator
CN101825391A (en) * 2009-03-06 2010-09-08 南通天义环保能源设备有限公司 Device for drying hydrous waste plastic
CN202238868U (en) * 2011-09-29 2012-05-30 湖南现代威保特环保科技有限公司 Harmless dewaterer
CN102564115A (en) * 2011-12-27 2012-07-11 深圳市盛鑫源环保科技技术有限公司 Rotary kiln air supply device
GB2485180B (en) * 2010-11-04 2012-09-26 Chinook Sciences Ltd Improvements in waste processing

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1133965A (en) * 1995-04-11 1996-10-23 拜尔公司 Device for supplying gas to rotary kilns
US5779468A (en) * 1995-04-11 1998-07-14 Bayer Aktiengesellschaft Device for supplying gas to rotary kilns
CN201032153Y (en) * 2007-02-07 2008-03-05 史金麟 Honeycomb grate incinerator
CN101050859A (en) * 2007-04-17 2007-10-10 史金麟 Method for gasifying and burning domestic garbage
CN101825391A (en) * 2009-03-06 2010-09-08 南通天义环保能源设备有限公司 Device for drying hydrous waste plastic
GB2485180B (en) * 2010-11-04 2012-09-26 Chinook Sciences Ltd Improvements in waste processing
CN202238868U (en) * 2011-09-29 2012-05-30 湖南现代威保特环保科技有限公司 Harmless dewaterer
CN102564115A (en) * 2011-12-27 2012-07-11 深圳市盛鑫源环保科技技术有限公司 Rotary kiln air supply device

Also Published As

Publication number Publication date
CN104344689A (en) 2015-02-11

Similar Documents

Publication Publication Date Title
CN105368496B (en) A kind of biomass gasification and gas-supply coproduction electricity, charcoal, heat, the process of fertilizer
CN102936507B (en) Poly-generation device and method for biomass pyrolysis
CN104312600A (en) Sludge pyrolysis and gasification treatment process and sludge pyrolysis and gasification treatment system
JP6124494B1 (en) Plant biomass semi-carbide production equipment
CN103939911B (en) One way of life refuse gasification processes and heat-energy utilizing device with burning
CN104923042B (en) A kind of partition rotary kiln device of fume-dehydrating
CN106642139A (en) Domestic refuse pyrolysis and gasification and fly ash direct melting device and use method thereof
CN106949480A (en) A kind of pyrogenation incinerator
CN107138515A (en) A kind of heat supply method of energy-saving and emission-reduction
CN104344689B (en) A kind of method of Hot-blast Heating house refuse transpiring moisture and drying unit thereof
CN105465793B (en) Double-deck stoker fired grate formula refuse gasification burns double boiler electricity generation system
CN107163953A (en) A kind of biomass and carbon containing thermal decomposition of organic wastes rotary furnace and thermal decomposition product recovery system
CN105131994B (en) Broken bituminous coal stalk prepares particle nitrogen-free hot gas method for destructive distillation
JP5843952B1 (en) Method and apparatus for semi-carbonizing dried product
CN211976884U (en) Domestic waste drying system
CN103333703B (en) Drying or low-temperature destructive distillation method and device of brown coal or low-deterioration long flame coal
CN206478647U (en) House refuse dehumidifying pyrolysis gasifying device
CN107876542A (en) A kind of method of revolving bed pyrolysis oven and processing rubbish
CN105402738B (en) Double-deck stoker fired grate formula refuse gasification incinerator and its double boiler system
CN104498104B (en) Biological flue gas boiler of feeding production method and its system and device
CN204786428U (en) Multicavity room domestic waste pyrolysis treatment complete sets
CN204125429U (en) A kind of two-section type is without pitch coal gas producer
CN206637620U (en) A kind of pyrogenation incinerator
CN104654768A (en) Biogas hot air drying process
CN205833820U (en) The processing system of one way of life rubbish

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
TR01 Transfer of patent right

Effective date of registration: 20171215

Address after: 213300 Xingcheng West Road, No. 290, Liyang City, Liyang City, Changzhou, Jiangsu

Patentee after: Liyang City Yuanjun Biomass Gas Co. Ltd.

Address before: 213300 Jiangsu, Liyang workers Village, building three, unit 601, room 4

Co-patentee before: Yin Meifang

Patentee before: Shi Jinlin

Co-patentee before: Shi Huiyuan

TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20191210

Address after: 213300, room two, unit 13, block 1, Kunlun garden, Liyang, Jiangsu,, Changzhou

Patentee after: Shi Huiyuan

Address before: 213300 Room 8301, 290 Xingcheng West Road, Bieqiao Town, Liyang City, Changzhou City, Jiangsu Province

Patentee before: Liyang City Yuanjun Biomass Gas Co. Ltd.

TR01 Transfer of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20160824

Termination date: 20201016

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