JPH0464811A - Refuse incinerator - Google Patents
Refuse incineratorInfo
- Publication number
- JPH0464811A JPH0464811A JP2176079A JP17607990A JPH0464811A JP H0464811 A JPH0464811 A JP H0464811A JP 2176079 A JP2176079 A JP 2176079A JP 17607990 A JP17607990 A JP 17607990A JP H0464811 A JPH0464811 A JP H0464811A
- Authority
- JP
- Japan
- Prior art keywords
- waste
- heat
- refuse
- garbage
- container
- 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.)
- Pending
Links
- 238000011084 recovery Methods 0.000 claims abstract description 22
- 238000002485 combustion reaction Methods 0.000 claims abstract description 18
- 239000010813 municipal solid waste Substances 0.000 claims description 37
- 239000002699 waste material Substances 0.000 claims description 32
- 238000005338 heat storage Methods 0.000 claims description 22
- 238000002844 melting Methods 0.000 claims description 15
- 230000008018 melting Effects 0.000 claims description 15
- 239000011232 storage material Substances 0.000 claims description 14
- 229910052751 metal Inorganic materials 0.000 claims description 13
- 239000002184 metal Substances 0.000 claims description 13
- 150000003839 salts Chemical class 0.000 claims description 13
- 239000012530 fluid Substances 0.000 claims description 11
- 238000010438 heat treatment Methods 0.000 claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- 229910052745 lead Inorganic materials 0.000 claims description 6
- 230000007246 mechanism Effects 0.000 claims description 6
- 229910052718 tin Inorganic materials 0.000 claims description 6
- 230000006835 compression Effects 0.000 claims description 4
- 238000007906 compression Methods 0.000 claims description 4
- 150000002739 metals Chemical class 0.000 claims description 4
- 239000012768 molten material Substances 0.000 claims description 4
- 238000003825 pressing Methods 0.000 claims description 4
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 3
- 229910052787 antimony Inorganic materials 0.000 claims description 3
- 229910052785 arsenic Inorganic materials 0.000 claims description 3
- 229910052797 bismuth Inorganic materials 0.000 claims description 3
- 229910052793 cadmium Inorganic materials 0.000 claims description 3
- 238000000926 separation method Methods 0.000 claims description 3
- -1 Bacl Chemical compound 0.000 claims description 2
- 230000002093 peripheral effect Effects 0.000 claims description 2
- 230000032258 transport Effects 0.000 claims 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 6
- 229910052799 carbon Inorganic materials 0.000 abstract description 5
- 230000009965 odorless effect Effects 0.000 abstract description 4
- 238000000034 method Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 10
- 230000000694 effects Effects 0.000 description 4
- 238000007711 solidification Methods 0.000 description 4
- 230000008023 solidification Effects 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 3
- 231100000252 nontoxic Toxicity 0.000 description 3
- 230000003000 nontoxic effect Effects 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 2
- 229920003002 synthetic resin Polymers 0.000 description 2
- 239000000057 synthetic resin Substances 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 229910017053 inorganic salt Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 235000010289 potassium nitrite Nutrition 0.000 description 1
- 238000003303 reheating Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 235000010344 sodium nitrate Nutrition 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/14—Thermal energy storage
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野j
本発明は、マンション、中小規模の事業所等に設置する
ごみ焼却炉に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Use] The present invention relates to a waste incinerator installed in condominiums, small and medium-sized business establishments, etc.
従来、マンション、中小規模の事業所等においては、ご
みを清掃車によって回収していた。Conventionally, garbage was collected by cleaning trucks in condominiums, small and medium-sized businesses, etc.
〔発明が解決しようとする課題1
しかし、上述の従来装置は、ごみを単に、清掃車によっ
て回収するだけであるため、熱、炭素等が無駄になると
いう問題点があった。[Problem to be Solved by the Invention 1] However, the above-mentioned conventional apparatus has a problem in that heat, carbon, etc. are wasted because the garbage is simply collected by a cleaning vehicle.
そこで、本発明は、ごみを無騒音で燃焼し、無毒、無臭
な排気ガスを排気し、これによりごみの体積を減少させ
、さらに、燃焼による熱を回収し、炉壁を保護し、炭素
等を回収できるごみ焼却炉を捉供することを目的とする
。Therefore, the present invention burns waste noiselessly, exhausts non-toxic and odorless exhaust gas, thereby reducing the volume of waste, recovers heat from combustion, protects the furnace wall, and removes carbon and other substances. The aim is to acquire and provide waste incinerators that can collect waste.
[課題を解決するだめの手段1
本発明は、ごみが投入されるごみ投入口と、該ごみ投入
口に連通し、該ごみが第1の搬送装置により搬送される
下部搬送路と、該下部搬送路の端部に接続し、連通し、
はぼ垂直方向に立設され、空気孔が設けられる筒部と、
該筒部まで搬送された該ごみを押圧圧縮する圧縮装置と
、該押圧圧縮されたごみを該筒部内で押し上げる押し上
げ装置と、該押し上げられたごみを該筒部内で加熱して
、燃焼させる燃焼装置と、該押し」二げられ、燃焼され
たごみから熱を該筒部内で回収し、該筒部外で蓄熱する
熱回収蓄熱装置と、該燃焼されたごみが、該筒部の上部
から第2の搬送装置により搬送される上部搬送路と、該
燃焼により発生した排気ガスを排気し、該上部搬送路に
設けられた排気装置と、該上部搬送路を通過した該ごみ
を分別回収する分別回収装置と、から成ることを特徴と
するごみ焼却炉である。[Means for Solving the Problems 1] The present invention provides a garbage input port into which garbage is input, a lower conveyance path communicating with the garbage input port and through which the garbage is conveyed by a first conveyance device, and a lower conveyance path in which the garbage is conveyed by a first conveyance device. Connects and communicates with the end of the conveyance path,
a cylindrical portion that stands vertically and is provided with air holes;
A compression device that presses and compresses the garbage that has been conveyed to the cylindrical portion, a push-up device that pushes up the compressed garbage within the cylindrical portion, and combustion that heats and burns the pushed up garbage within the cylindrical portion. a heat recovery/storage device that recovers heat from the pressed and burned waste within the cylindrical part and stores the heat outside the cylindrical part; An upper conveyance path that is conveyed by a second conveyance device, exhausts the exhaust gas generated by the combustion, and separates and collects the waste that has passed through the exhaust device provided in the upper conveyance path and the upper conveyance path. This is a waste incinerator characterized by comprising a separation and collection device.
本発明によれば、筒部内でごみを無騒音で燃焼し、無毒
、無臭な排気ガスを排気し、これによりごみの体積を減
少させる。さらに、熱回収蓄熱装置により燃焼による熱
を回収して、温度を制御し、炉壁を保護し、分別回収装
置により炭素等を回収できる。According to the present invention, trash is burned noiselessly within the cylinder, and non-toxic and odorless exhaust gas is exhausted, thereby reducing the volume of trash. Furthermore, heat from combustion can be recovered by a heat recovery and storage device to control the temperature and protect the furnace wall, and carbon and the like can be recovered by a separation recovery device.
以下、本発明を図面を参照してその実施例に基づいて説
明する。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below based on embodiments with reference to the drawings.
第1図は本発明の一実施例の断面図、第2図は第1図の
A−A線矢視図である。FIG. 1 is a sectional view of one embodiment of the present invention, and FIG. 2 is a view taken along the line A--A in FIG.
投入口1からごみ2が投入され、下部搬送路3がごみ投
入口1に連通し、ごみ2が第1の搬送装置4により搬送
される。Garbage 2 is inputted from the input port 1 , the lower conveyance path 3 communicates with the garbage input port 1 , and the garbage 2 is conveyed by the first conveyance device 4 .
また、第1の搬送装置4はごみ2を搬送する複数対の開
閉するドア機構から成るが、スクリュウ機構、あるいは
、ごみ2を押圧することにより搬送する押圧機構から構
成されてもよく、その構造は、特に、限定されない。Further, the first conveyance device 4 is composed of a plurality of pairs of door mechanisms that open and close to convey the garbage 2, but it may also be constituted by a screw mechanism or a pressing mechanism that conveys the garbage 2 by pressing it. is not particularly limited.
また、下部搬送路3内においてごみ2を加熱する加熱装
置15と、加熱されたごみ2から溶融した溶融物を回収
する溶融物回収装置16を備える。It also includes a heating device 15 that heats the waste 2 in the lower conveyance path 3, and a molten material recovery device 16 that collects molten material from the heated waste 2.
溶融物回収装置16はごみ2が落下しないように篩20
を設ける。The melt recovery device 16 is equipped with a sieve 20 to prevent the garbage 2 from falling.
will be established.
この加熱装置15による加熱温度を順次変化させるとご
み2の中の合成樹脂が順次溶解して、溶融物回収装置1
6へ落下し、蓄積される。When the heating temperature by this heating device 15 is sequentially changed, the synthetic resin in the garbage 2 is sequentially melted, and the melt recovery device 1
It falls to 6 and accumulates.
ここで、合成樹脂が除去されて、ごみ2の燃焼時に発生
ずる塩化ガス(塩酸)、ぶつ化ガス等の発生量を減少さ
せる。Here, the synthetic resin is removed to reduce the amount of chloride gas (hydrochloric acid), oxidized gas, etc. generated when the garbage 2 is burned.
筒部5は下部搬送路3の端部6に接続し、連通し、はぼ
垂直方向に立設され、空気孔7が設けられる。The cylindrical portion 5 is connected to and communicates with the end portion 6 of the lower conveyance path 3, is erected in a substantially vertical direction, and is provided with an air hole 7.
圧縮装置8は筒部5まで搬送されたごみ2を押圧圧縮し
、シリンダ98等から成る押し上げ装置9は押圧圧縮さ
れたごみ2を筒部5内で順次押し上げる。The compression device 8 presses and compresses the garbage 2 that has been conveyed to the cylindrical portion 5, and the pushing device 9, which includes a cylinder 98 and the like, sequentially pushes up the press-compressed garbage 2 within the cylindrical portion 5.
次に、ヒーター、電磁波加熱装置等から成る燃焼装置1
0は押し上げられたごみ2を筒部5内で加熱して、燃焼
を促進させ、熱回収蓄熱装置21で燃焼されたごみ2か
ら熱を筒部5内で回収し、筒部5外で蓄熱する。Next, a combustion device 1 consisting of a heater, an electromagnetic wave heating device, etc.
0 heats the pushed-up garbage 2 inside the cylindrical part 5 to promote combustion, recovers heat from the burned garbage 2 in the heat recovery and storage device 21 within the cylindrical part 5, and stores the heat outside the cylindrical part 5. do.
燃焼装置10の設ける箇所、数は適宜調整される。The location and number of combustion devices 10 are adjusted as appropriate.
熱回収蓄熱装置21については後述する。The heat recovery heat storage device 21 will be described later.
次に、上部搬送路12を燃焼されたごみ2が、筒部5の
上部13から第2の搬送装置31により押圧されて搬送
される。Next, the burned waste 2 in the upper transport path 12 is pressed and transported from the upper part 13 of the cylindrical part 5 by the second transport device 31 .
さらに、分別回収装置14は上部搬送路12を搬送され
たごみ2を篩32により分別して、容器33a、33b
により回収する。 さらに、この容器33aのごみを清
掃車等で回収する。Furthermore, the sorting and collection device 14 separates the garbage 2 conveyed through the upper conveyance path 12 using a sieve 32, and separates the garbage 2 into containers 33a and 33b.
Collected by Furthermore, the garbage in this container 33a is collected by a cleaning vehicle or the like.
また、容器33bに篩32により分別回収された炭素粉
な再加熱用の燃料等に用いる。In addition, carbon powder, which is separated and recovered by the sieve 32 in the container 33b, is used as fuel for reheating.
また、排気装置34は上部搬送路12に設けられ、この
燃焼により発生した排気ガスを排気する。Further, an exhaust device 34 is provided in the upper conveyance path 12 to exhaust exhaust gas generated by this combustion.
また、この排気ガス中の臭気、塵、NO8等を、排気ガ
スを燃焼させたり、電気的に加熱することにより除去す
る。Further, odor, dust, NO8, etc. in the exhaust gas are removed by burning the exhaust gas or electrically heating it.
さらに、中空内部に加熱体17を有し、周壁に空気孔1
8が設けられ、筒部5の底部から立設されたガイドパイ
プ19を設ける。Furthermore, it has a heating body 17 inside the hollow, and air holes 1 in the peripheral wall.
8 is provided, and a guide pipe 19 is provided that stands up from the bottom of the cylindrical portion 5.
このガイドパイプ19は筒部5内においてごみ2を上方
へ誘導するガイドとしての役割を果たす。This guide pipe 19 serves as a guide for guiding the dust 2 upward within the cylindrical portion 5.
筒部5の空気孔7およびガイドパイプ19の空気孔18
がら空気が噴出されることにより、ごみ2が燃焼され、
また、空気孔7および空気孔】8からの空気が遮断され
、あるいは、窒素等が噴出されることにより燃焼が抑制
され、所定温度に制御される。Air hole 7 of cylinder part 5 and air hole 18 of guide pipe 19
Garbage 2 is combusted by the air being blown out,
In addition, combustion is suppressed by blocking air from the air holes 7 and 8, or by blowing out nitrogen or the like, and the temperature is controlled to a predetermined temperature.
第3図は本実施例を構成する熱回収蓄熱装置21の構成
図である。FIG. 3 is a configuration diagram of the heat recovery and storage device 21 constituting this embodiment.
次に、熱回収蓄熱装置21は、筒部5の内壁を構成する
第1の容器11と、第1の容器11に充填される流体状
熱媒体と、筒部5の外部に設けられる第2の容器23と
、第1の容器11に接続連通され、第2の容器23内を
通過するように設けられるパイプ24と、第1の容器l
l内で加熱された流体状熱媒体がパイプ24内をポンプ
25により第2の容器23内を循環されたときに、流体
状熱媒体から熱を吸収し、蓄熱する蓄熱材26とから成
る。Next, the heat recovery heat storage device 21 includes a first container 11 forming the inner wall of the cylindrical portion 5 , a fluid heat medium filled in the first container 11 , and a second container provided outside the cylindrical portion 5 . a pipe 24 connected to and communicating with the first container 11 and passing through the second container 23;
When the fluid heat medium heated in the second container 23 is circulated through the pipe 24 by the pump 25, the heat storage material 26 absorbs heat from the fluid heat medium and stores the heat.
パイプ24は流体制御用の弁24を有する。The pipe 24 has a valve 24 for fluid control.
第1の容器ll内の流体状熱媒体が筒部5内におけるご
み2の燃焼による熱を吸収する。The fluid heat medium in the first container 11 absorbs heat due to the combustion of the waste 2 in the cylindrical portion 5.
次に、この熱回収蓄熱装置21の蓄熱材26は水、無機
塩類、または、低融点金属から成る。Next, the heat storage material 26 of this heat recovery and heat storage device 21 is made of water, inorganic salts, or a low melting point metal.
次に、この無機塩類はNaN0z 、NaNO3、KN
O3、KNO2、Nacl、Bacl、Kclの内の1
以上から構成されても良い。Next, these inorganic salts are NaN0z, NaNO3, KN
One of O3, KNO2, Nacl, Bacl, Kcl
It may be configured from the above.
また、この無機塩類はこの無機塩類に水分が加わった水
溶液から構成されても良い。Further, the inorganic salts may be composed of an aqueous solution in which water is added to the inorganic salts.
この低融点金属はSn、および、Pbの内の1以上から
成る。This low melting point metal consists of one or more of Sn and Pb.
また、この低融点金属はSn、および、Pbの内の1以
上と、Bi、Sb、As、Cdの内の1以上とから構成
されても良い。Further, this low melting point metal may be composed of one or more of Sn and Pb, and one or more of Bi, Sb, As, and Cd.
流体状熱媒体は水、油、溶融液等から成る。The fluid heat carrier consists of water, oil, molten liquid, etc.
第2の容器23は外壁板と、内壁板とから成り、この間
は真空状態に保持され、あるいは、重の壁板から構成さ
れて断熱効果を有する。The second container 23 is made up of an outer wall plate and an inner wall plate, which are maintained in a vacuum state, or are made of heavy wall plates to have a heat insulating effect.
本実施例では、蓄熱材26は無機塩類、または、低融点
金属から構成されることが好適であるが、水を用いても
良い。In this embodiment, the heat storage material 26 is preferably composed of inorganic salts or low melting point metals, but water may also be used.
常温ではこの無機塩類、または、低融点金属から構成さ
れる蓄熱材26は固体状であるが、流体状熱媒体の熱に
より蓄熱され、蓄熱を続行し、所定温度に達すると溶解
を開始し、さらに、蓄熱を続行する。At room temperature, the heat storage material 26 composed of inorganic salts or low melting point metals is solid, but heat is stored by the heat of the fluid heat medium, continues to store heat, and starts melting when a predetermined temperature is reached. Furthermore, heat storage continues.
蓄熱材26の全部が溶解した後も蓄熱が続行され、さら
に、温度が上昇する。Even after all of the heat storage material 26 is melted, heat storage continues, and the temperature further increases.
その後、逆に、パイプ内を循環する流体状熱媒体を蓄熱
材26に蓄熱された熱により加熱し、所定温度まで低下
すると固体化を開始し、全体が凝固潜熱を発生しながら
、固体化されるまで、同じ温度での給熱を続行する。Then, conversely, the fluid heat medium circulating inside the pipe is heated by the heat stored in the heat storage material 26, and when the temperature drops to a predetermined temperature, solidification begins, and the entire body solidifies while generating latent heat of solidification. Continue supplying heat at the same temperature until
凝固が完了すると加熱温度は徐々に低下する。Once solidification is complete, the heating temperature is gradually lowered.
このため、無機塩類、または、低融点金属から構成され
る蓄熱材は水に対して、同じ容積での蓄熱容量が大きく
、蓄熱効率が高く、装置自体の容積を小型化できる。Therefore, a heat storage material made of an inorganic salt or a low melting point metal has a large heat storage capacity in the same volume as water, has high heat storage efficiency, and can reduce the volume of the device itself.
密閉部材27と蓄熱材26との開の空間28は中性ガス
であるN2、不活性ガスであるAr等により充填される
。The open space 28 between the sealing member 27 and the heat storage material 26 is filled with neutral gas N2, inert gas Ar, or the like.
この中性ガス、不活性ガスにより蓄熱材26および第2
の容器23の内壁の酸化が防止される。The heat storage material 26 and the second
Oxidation of the inner wall of the container 23 is prevented.
この無機塩類は、例えば、N a N 02、NaNO
s 、KNOz 、KNOz 、Nacl、Bacl、
Kclの内の1以上から成る。These inorganic salts include, for example, NaN02, NaNO
s, KNOz, KNOz, Nacl, Bacl,
Consisting of one or more of Kcl.
さらに、無機塩類は無機塩類に水分が加わった水溶液か
ら構成されても良い。Furthermore, the inorganic salts may be composed of an aqueous solution in which water is added to the inorganic salts.
低融点金属は、例えば、Sn、および、Pbの内の1以
上から成る。The low melting point metal includes, for example, one or more of Sn and Pb.
さらに、低融点金属はSn、および、Pbの内の1以上
と、Bi、Sb、As、Cdの内の1以上とから構成さ
れても良い。Furthermore, the low melting point metal may be composed of one or more of Sn and Pb, and one or more of Bi, Sb, As, and Cd.
以上例示した、蓄熱材26の材料の混合割合等により蓄
熱材の溶解温度を変更できる。The melting temperature of the heat storage material can be changed by changing the mixing ratio of the materials of the heat storage material 26 as exemplified above.
また、無機塩類、あるいは、低融点金属の構成成分の配
合によって任意の凝固温度を実現することができる。Furthermore, any desired solidification temperature can be achieved by mixing inorganic salts or low melting point metal components.
蓄熱材26である無機塩類、低融点金属の材料は上述の
ものに限定されないことはもちろんである。Of course, the materials such as inorganic salts and low melting point metals that are the heat storage material 26 are not limited to those described above.
また、以上の本実施例は床29上に支台30により支え
られる。Further, the present embodiment described above is supported by a support 30 on the floor 29.
また、燃焼装置10、加熱装置15および加熱体17に
おいては深夜電力を用いることが経済的である。Furthermore, it is economical to use late-night electricity in the combustion device 10, heating device 15, and heating element 17.
[発明の効果1
本発明は以上説明したように、筒部内でごみを無騒音で
燃焼し、無毒、無臭な排気ガスを排気し、これによりご
みの体積を減少させる。さらに、熱回収蓄熱装置により
燃焼による熱を回収し、温度を制御し、炉壁を保護し、
分別回収装置により炭素等を回収できるという効果を奏
する。[Advantageous Effects of the Invention 1] As explained above, the present invention burns waste noiselessly within the cylindrical portion, exhausts non-toxic and odorless exhaust gas, and thereby reduces the volume of waste. In addition, a heat recovery and storage device recovers heat from combustion, controls temperature, protects the furnace wall,
This has the effect that carbon, etc. can be recovered by the separate recovery device.
第1図は本発明の一実施例の断面図、第2図は第1図の
A−A線矢視図、第3図は本実施例を構成する熱回収蓄
熱装置の構成図である。
1・・・ごみ投入口 2・・・ごみ3・・・下部搬
送路 4・・・第1の搬送装置5・・・筒部
8・・・圧縮装置9・・・押し上げ装置 14
・・・分別回収装置19・・・ガイドパイプ 21・・
・熱回収装置31・・・第2の搬送装置FIG. 1 is a sectional view of an embodiment of the present invention, FIG. 2 is a view taken along the line A--A in FIG. 1, and FIG. 3 is a configuration diagram of a heat recovery and storage device constituting this embodiment. 1... Garbage input port 2... Garbage 3... Lower conveyance path 4... First conveyance device 5... Cylinder part
8... Compression device 9... Pushing device 14
...Separate collection device 19...Guide pipe 21...
・Heat recovery device 31...second conveyance device
Claims (1)
と、 該燃焼されたごみが、該筒部の上部から第 2の搬送装置により搬送される上部搬送路 と、 該燃焼により発生した排気ガスを排気し、 該上部搬送路に設けられた排気装置と、 該上部搬送路を通過した該ごみを分別回収 する分別回収装置と、 から成ることを特徴とするごみ焼却炉。 2 該下部搬送路内において該ごみを加熱する加熱装
置と、 該加熱されたごみから溶融した溶融物を回 収する溶融物回収装置と、 を備えた請求項1記載のごみ焼却炉。 3 中空内部に加熱体を有し、周壁に空気孔が設けら
れ、該筒部の底部から立設されたガイドパイプを備えた
請求項1または2記載のごみ焼却炉。 4 該第1の搬送装置は該ごみを搬送する複数対の開
閉するドア機構から成る請求項1ないし3のいずれかに
記載のごみ焼却炉。 5 該第1の搬送装置は該ごみを搬送するスクリュウ
機構から成る請求項1ないし3のいずれかに記載のごみ
焼却炉。 6 該第1の搬送装置は該ごみを押圧することにより
搬送する押圧機構から成る請求項 1ないし3のいずれかに記載のごみ焼却炉。 7 該熱回収蓄熱装置は、 該筒部の内壁を構成する第1の容器と、 該第1の容器内に充填される流体状熱媒体 と、 該筒部の外部に設けられる第2の容器と、 該第1の容器に接続連通され、第2の容器 内を通過するように設けられるパイプと、 該第1の容器内で加熱された流体状熱媒体 が該パイプ内をポンプにより該第2の容器内を循環され
たときに、該流体状熱媒体から熱を吸収し、蓄熱する蓄
熱材と、 から成る請求項1ないし6のいずれかに記 載のごみ焼却炉。 8 該蓄熱材は水、無機塩類、または、低融点金属か
ら成る請求項7記載のごみ焼却炉。 9 該無機塩類はNaNO_2、NaNO_3、KN
O_3、KNO_2、Nacl、Bacl、Kclの内
の1以上から成る請求項8記載のごみ焼却炉。 10 該低融点金属はSn、および、Pbの内の1以
上から成る請求項8または9記載のごみ焼却炉。 11 該低融点金属はSn、および、Pbの内の1以
上と、Bi、Sb、As、Cdの内の1以上とから成る
請求項8または9記載のごみ焼却炉。[Scope of Claims] 1. A garbage input port into which garbage is input; a lower conveyance path communicating with the garbage input port and through which the garbage is conveyed by a first conveyance device; and an end portion of the lower conveyance path. A cylindrical part that is connected and communicated, stands upright in a substantially vertical direction, and is provided with air holes; a compression device that presses and compresses the waste that has been conveyed to the cylindrical part; a combustion device that heats and burns the pushed up waste inside the cylindrical section; a combustion device that collects heat from the pushed up and burned trash within the cylindrical section and stores it outside the cylindrical section; an upper conveyance path through which the burned waste is conveyed from the upper part of the cylindrical part by a second conveyance device; and an upper conveyance path through which exhaust gas generated by the combustion is exhausted and which is conveyed to the upper conveyance path. A waste incinerator characterized by comprising: an exhaust device provided therein; and a separation and recovery device that separates and collects the waste that has passed through the upper conveyance path. 2. The garbage incinerator according to claim 1, comprising: a heating device that heats the garbage in the lower conveyance path; and a molten material recovery device that recovers molten material from the heated waste. 3. The waste incinerator according to claim 1 or 2, further comprising a heating body in the hollow interior, an air hole provided in the peripheral wall, and a guide pipe erected from the bottom of the cylindrical portion. 4. The waste incinerator according to any one of claims 1 to 3, wherein the first transport device comprises a plurality of pairs of opening/closing door mechanisms for transporting the waste. 5. The waste incinerator according to any one of claims 1 to 3, wherein the first transport device comprises a screw mechanism for transporting the waste. 6. The waste incinerator according to any one of claims 1 to 3, wherein the first transport device comprises a pressing mechanism that transports the waste by pressing it. 7. The heat recovery heat storage device includes: a first container forming an inner wall of the cylindrical portion; a fluid heat medium filled in the first container; and a second container provided outside the cylindrical portion. a pipe connected to and communicated with the first container and passing through the second container; a fluid heat medium heated in the first container being pumped through the pipe into the second container; 7. The waste incinerator according to any one of claims 1 to 6, comprising: a heat storage material that absorbs heat from the fluid heat medium and stores the heat when it is circulated in the second container. 8. The waste incinerator according to claim 7, wherein the heat storage material is made of water, inorganic salts, or low melting point metals. 9 The inorganic salts are NaNO_2, NaNO_3, KN
The waste incinerator according to claim 8, comprising one or more of O_3, KNO_2, Nacl, Bacl, and Kcl. 10. The waste incinerator according to claim 8 or 9, wherein the low melting point metal comprises one or more of Sn and Pb. 11. The waste incinerator according to claim 8 or 9, wherein the low melting point metal comprises one or more of Sn and Pb, and one or more of Bi, Sb, As, and Cd.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2176079A JPH0464811A (en) | 1990-07-03 | 1990-07-03 | Refuse incinerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2176079A JPH0464811A (en) | 1990-07-03 | 1990-07-03 | Refuse incinerator |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0464811A true JPH0464811A (en) | 1992-02-28 |
Family
ID=16007354
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2176079A Pending JPH0464811A (en) | 1990-07-03 | 1990-07-03 | Refuse incinerator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0464811A (en) |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4919588A (en) * | 1972-02-11 | 1974-02-21 | ||
JPS5065063A (en) * | 1973-10-10 | 1975-06-02 | ||
JPS5199875A (en) * | 1975-02-28 | 1976-09-03 | Kubota Ltd | KOKARORII HAIKIBUTSUNO SHOKYAKURO |
JPS5248626U (en) * | 1975-10-04 | 1977-04-06 | ||
JPS5488671A (en) * | 1977-12-26 | 1979-07-13 | Hitachi Zosen Corp | Method of re-combusting uncombusted matters in waste combusting furnace |
JPS5514423A (en) * | 1978-07-17 | 1980-01-31 | Babcock Hitachi Kk | Wastes feeding apparatus |
JPS62166216A (en) * | 1986-01-17 | 1987-07-22 | Ebara Corp | Method and device for recovering heat from fluidized bed |
JPH0210013A (en) * | 1988-06-28 | 1990-01-12 | Matsushita Seiko Co Ltd | Refuse disposal device |
-
1990
- 1990-07-03 JP JP2176079A patent/JPH0464811A/en active Pending
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4919588A (en) * | 1972-02-11 | 1974-02-21 | ||
JPS5065063A (en) * | 1973-10-10 | 1975-06-02 | ||
JPS5199875A (en) * | 1975-02-28 | 1976-09-03 | Kubota Ltd | KOKARORII HAIKIBUTSUNO SHOKYAKURO |
JPS5248626U (en) * | 1975-10-04 | 1977-04-06 | ||
JPS5488671A (en) * | 1977-12-26 | 1979-07-13 | Hitachi Zosen Corp | Method of re-combusting uncombusted matters in waste combusting furnace |
JPS5514423A (en) * | 1978-07-17 | 1980-01-31 | Babcock Hitachi Kk | Wastes feeding apparatus |
JPS62166216A (en) * | 1986-01-17 | 1987-07-22 | Ebara Corp | Method and device for recovering heat from fluidized bed |
JPH0210013A (en) * | 1988-06-28 | 1990-01-12 | Matsushita Seiko Co Ltd | Refuse disposal device |
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