JP2002035729A - Method for producing carbide made from refuse derived fuel as raw material and apparatus therefor - Google Patents
Method for producing carbide made from refuse derived fuel as raw material and apparatus thereforInfo
- Publication number
- JP2002035729A JP2002035729A JP2000223333A JP2000223333A JP2002035729A JP 2002035729 A JP2002035729 A JP 2002035729A JP 2000223333 A JP2000223333 A JP 2000223333A JP 2000223333 A JP2000223333 A JP 2000223333A JP 2002035729 A JP2002035729 A JP 2002035729A
- Authority
- JP
- Japan
- Prior art keywords
- carbide
- cooling
- solid fuel
- refuse
- temperature
- 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
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
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- 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
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Landscapes
- Processing Of Solid Wastes (AREA)
- Coke Industry (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
Description
【０００１】[0001]
【発明が属する技術分野】この発明は、 ごみを破砕、乾
燥および成形して得た固形燃料から炭化物を製造する方
法およびその装置に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and apparatus for producing carbide from solid fuel obtained by crushing, drying and molding refuse.
【０００２】[0002]
【従来の技術】近年、 廃棄物、いわゆるごみから可燃ご
みを選別して回収したのち、このゴミを破砕、乾燥およ
び成形して固形燃料とする、ごみの処理および利用技術
が、種々開発されている。例えば、このような技術とし
て、特許第2865541 号、同第2981399 号および特開平８
−86569 号公報などを挙げることができる。2. Description of the Related Art In recent years, various technologies for treating and utilizing garbage have been developed in which combustible garbage is sorted and collected from waste, so-called garbage, and then the garbage is crushed, dried and formed into a solid fuel. I have. For example, Japanese Patent Nos. 2865541 and 2981399 and Japanese Patent Application Laid-Open No.
-86569.
【０００３】すなわち、都市ごみ、家庭ごみ、産業廃棄
物および一般廃棄物などのごみを、破砕した後、ごみ中
の水分を減少するために乾燥を行い、金属、ガラスおよ
び陶器類等を除去する選別を経て、所定の形状、例えば
クレヨン形状などに成形し、固形燃料とするものであ
る。That is, after crushing garbage such as municipal garbage, household garbage, industrial waste and municipal waste, the garbage is dried to reduce the water content in the garbage to remove metals, glass, pottery and the like. After sorting, it is formed into a predetermined shape, for example, a crayon shape, to obtain a solid fuel.
【０００４】このごみ固形燃料は、各種施設の冷暖房用
の熱源として、また発電用の燃料として、利用されてい
るが、その利用に当っては、ごみ固形燃料に適した設備
の新設や、既存設備の改造などの、設備投資が必要とな
る。一方で、日々発生するごみの量は増加の一途を辿っ
ており、これに比例して、ごみ固形燃料を増産すること
が、環境保全の観点から望まれている。[0004] The solid waste fuel is used as a heat source for cooling and heating of various facilities and as a fuel for power generation. Equipment investment such as equipment remodeling is required. On the other hand, the amount of refuse generated every day is steadily increasing, and it is desired to increase the production of refuse solid fuel in proportion to this from the viewpoint of environmental conservation.
【０００５】ところが、上記のように、ごみ固形燃料を
活用するための設備が十分に用意されているとはいえな
い現状にあって、ごみ固形燃料を単に増産しても無意味
であるために、ごみ固形燃料の活用の場を新たに開拓し
て、その消費を促進する必要がある。[0005] However, as described above, in the present situation where facilities for utilizing solid waste fuel are not sufficiently prepared, simply increasing the amount of solid waste fuel is meaningless. Therefore, it is necessary to open up a new place to utilize solid fuel and promote its consumption.
【０００６】ここに、ごみ固形燃料を利用する技術とし
て、特開2000−80372 号公報には、ごみ固形燃料を乾留
して活性炭とすることが提案されている。この乾留処理
によって、ごみ固形燃料は有意義な活性炭として生まれ
変わるのである。[0006] Here, as a technique utilizing the solid waste fuel, Japanese Patent Application Laid-Open No. 2000-80372 proposes that the solid waste fuel be carbonized to be activated carbon. By this carbonization, the solid fuel is regenerated as meaningful activated carbon.
【０００７】[0007]
【発明が解決しようとする課題】ところで、炭化炉で乾
留直後の炭化物は高温であり、しかも微粉を含むことか
ら、完全に消火してから取り扱う必要がある。そのため
に、炭化炉から出た直後の炭化物を冷却してから貯留し
たり出荷したりすることが通例である。この冷却は、炭
化物が粉状であるため水を散布することが一般的である
が、所望の温度まで冷却するには多量の散水が必要であ
り、その結果炭化物の含水率が高くなることが問題であ
った。By the way, the carbide immediately after carbonization in the carbonization furnace has a high temperature and contains fine powder, so that it is necessary to completely extinguish the fire before handling. For this purpose, it is customary to cool and store or ship the carbide immediately after leaving the carbonization furnace. This cooling is generally performed by spraying water because the carbide is powdery.However, a large amount of water is required to cool to a desired temperature, and as a result, the water content of the carbide may increase. It was a problem.
【０００８】すなわち、炭化物の含水率が高いと、輸送
効率が悪くなる他、燃料として使用する場合に水分の蒸
発による熱量損失が大きくなり、また活性炭として使用
する場合には吸着性能が低下することになり、土壌改良
材として使用する場合には吸着性能の低下によって空気
含有率が減少して、土壌改良材としての機能が低下す
る、などの不都合が生じる。[0008] That is, when the water content of the carbide is high, the transport efficiency is deteriorated, and the calorific value loss due to the evaporation of water increases when used as fuel, and the adsorption performance decreases when used as activated carbon. When used as a soil conditioner, disadvantages such as a decrease in air content due to a decrease in adsorption performance and a decrease in the function as a soil conditioner occur.
【０００９】そこで、この発明は、乾留して得られた炭
化物の冷却を、その含水率の大幅な上昇をまねくことな
く、有利に達成する手法について提案することを目的と
する。Accordingly, an object of the present invention is to propose a method of advantageously achieving cooling of a carbide obtained by carbonization without causing a significant increase in the water content.
【００１０】[0010]
【課題を解決するための手段】すなわち、この発明の要
旨構成は、次のとおりである。 (1) ごみの破砕、乾燥および成形を経て所定の形状に加
工された、ごみ固形燃料を乾留して炭化物とし、次いで
該炭化物を500 ℃以上の温度の水蒸気にて冷却したの
ち、散水冷却を行うことを特徴とするごみ固形燃料を原
料とした炭化物の製造方法。That is, the gist of the present invention is as follows. (1) Waste solid fuel processed into a predetermined shape through crushing, drying and forming of the waste, is carbonized by carbonizing the solid fuel, and then the carbonized material is cooled with steam at a temperature of 500 ° C. or higher, and then cooled with water spray. A method for producing carbide using refuse solid fuel as a raw material.
【００１１】(2) 上記(1) において、水蒸気による冷却
を、炭化物の温度が600 ℃以下になるまで行うことを特
徴とするごみ固形燃料を原料とした炭化物の製造方法。(2) A method for producing a carbide from a solid refuse fuel as set forth in (1) above, wherein the cooling with steam is performed until the temperature of the carbide becomes 600 ° C. or less.
【００１２】(3) ごみの破砕、乾燥および成形を経て所
定の形状に加工された、ごみ固形燃料を乾留して炭化物
とし、次いで該炭化物を600 ℃以上の温度の含ＣＯ2 ガ
スにて冷却したのち、散水冷却を行うことを特徴とする
ごみ固形燃料を原料とした炭化物の製造方法。(3) The solid fuel, which has been processed into a predetermined shape through crushing, drying and molding of the refuse, is carbonized by carbonizing the refuse solid fuel, and then the char is cooled with a CO 2 -containing gas at a temperature of 600 ° C. or more. After that, a method for producing carbide using refuse solid fuel as a raw material, characterized by performing water spray cooling.
【００１３】(4) 上記(3) において、含ＣＯ2 ガスによ
る冷却を、炭化物の温度が700 ℃以下になるまで行うこ
とを特徴とするごみ固形燃料を原料とした炭化物の製造
方法。(4) The method for producing a carbide from a solid waste fuel as a raw material according to the above (3), wherein the cooling with the CO 2 -containing gas is performed until the temperature of the carbide becomes 700 ° C. or less.
【００１４】(5) 上記(3) または(4) において、含ＣＯ
2 ガスがごみ固形燃料を乾留する炭化炉からの排ガスで
あることを特徴とするごみ固形燃料を原料とした炭化物
の製造方法。(5) In the above (3) or (4), CO-containing
(2) A method for producing a carbide using refuse solid fuel as a raw material, wherein the two gases are exhaust gas from a carbonization furnace for carbonizing refuse solid fuel.
【００１５】(6) 内燃式の炭化炉の出側に、該炭化炉で
乾留された炭化物を搬送するスクリューコンベアを配置
し、該スクリューコンベアの経路に水蒸気または含ＣＯ
2 ガスの供給手段を有することを特徴とする炭化物の製
造装置。(6) A screw conveyor for transporting carbides carbonized in the carbonization furnace is disposed at the outlet side of the internal combustion type carbonization furnace, and steam or CO-containing water is supplied through the screw conveyor.
An apparatus for producing carbide, characterized by having two gas supply means.
【００１６】[0016]
【発明の実施の形態】以下、 この発明の方法について、
図面を参照して詳細に説明する。まず、この発明の方法
に直接使用する炭化物の製造装置を、図１に示す。該製
造装置は、内燃式の炭化炉１の出側に、該炭化炉１内に
て乾留処理された炭化物２を搬送するスクリューコンベ
ア３を配置し、該スクリューコンベア３の経路に水蒸気
または含ＣＯ2 ガスの供給手段、例えば炭化炉１からの
乾留ガスを燃焼した排ガスや蒸気の供給管４を配設して
成る。BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the method of the present invention will be described.
This will be described in detail with reference to the drawings. First, FIG. 1 shows an apparatus for producing carbide used directly in the method of the present invention. In the manufacturing apparatus, a screw conveyor 3 that conveys a char 2 that has been carbonized in the carbonization furnace 1 is disposed on the exit side of the internal combustion type carbonization furnace 1. Two gas supply means, for example, a supply pipe 4 for exhaust gas or steam obtained by burning carbonized gas from the carbonization furnace 1 is provided.
【００１７】ここで、炭化炉１に供給する、ごみ固形燃
料５は、 郡市ごみ、 家庭ごみなどの一般ごみ、 産業廃棄
物、 一般廃棄物、 および家電製品、自動車部品などを破
砕して得られたシュレッダーダストなどのごみから、 金
属類、 ガラスおよび陶磁器類を除去し、かくして得られ
た可燃物を主体とするごみを破砕し、 次いで乾燥後に再
度破砕してから、例えば棒状に成形されたものである。Here, the solid waste 5 supplied to the carbonization furnace 1 is obtained by crushing general waste such as county municipal waste, household waste, industrial waste, general waste, home electric appliances, automobile parts, and the like. Metals, glass, and ceramics are removed from waste such as shredder dust, and the flammable garbage thus obtained is crushed, then dried, crushed again, and then formed into, for example, a rod. It is.
【００１８】このごみ固形燃料５を炭化炉１に供給し、
ごみ固形燃料５を乾留することによって炭化物２を製造
する。この乾留処理は、例えば炉内への供給空気量を調
整して炉内の酸素濃度を１ vol％以下に制御するととも
に、炭化物から発生するダイオキシンの濃度を所定値以
下に制限するために、乾留温度を600 ℃以上、好ましく
は800 ℃以上に制御して行うことが好ましい。The solid fuel 5 is supplied to the carbonization furnace 1,
Carbide 2 is produced by carbonizing refuse solid fuel 5. This carbonization treatment involves, for example, controlling the amount of air supplied to the furnace to control the oxygen concentration in the furnace to 1 vol% or less, and restricting the concentration of dioxins generated from carbides to a predetermined value or less. It is preferable to control the temperature at 600 ° C. or higher, preferably 800 ° C. or higher.
【００１９】次いで、この炭化炉１で製造された炭化物
２を、 炭化炉１からスクリューコンベア３へ排出し、こ
のスクリューコンベア３を介して、炭化物２をその貯留
ホッパ６の下方まで搬送する。そして、炭化物２は、 ス
クリューコンベア３からベルトコンベア７へ切り出さ
れ、ベルトコンベア７を介して貯留ホッパ６に貯留され
る。Next, the carbide 2 produced in the carbonization furnace 1 is discharged from the carbonization furnace 1 to the screw conveyor 3, and the carbide 2 is transported to below the storage hopper 6 via the screw conveyor 3. Then, the carbide 2 is cut out from the screw conveyor 3 to the belt conveyor 7 and stored in the storage hopper 6 via the belt conveyor 7.
【００２０】さて、炭化炉１から排出された直後の炭化
物２は、1000〜800 ℃程度の温度を有し、消火する必要
があることから、炭化炉１から排出された炭化物２に対
して冷却を行う必要がある。そこで、上記供給管４から
スクリューコンベア３内に、500 ℃以上の水蒸気または
600 ℃以上の含ＣＯ2 ガスを導いて、スクリューコンベ
ア３内を移動する炭化物２に１次の冷却を施す。この１
次冷却によって、炭化物２を600 〜700 ℃程度まで冷却
する。Since the carbide 2 immediately after being discharged from the carbonization furnace 1 has a temperature of about 1000 to 800 ° C. and needs to be extinguished, the carbide 2 discharged from the carbonization furnace 1 is cooled. Need to do. Therefore, steam or 500 ° C. or higher steam is supplied from the supply pipe 4 into the screw conveyor 3.
By introducing a CO 2 -containing gas at a temperature of 600 ° C. or more, primary cooling is performed on the carbide 2 moving in the screw conveyor 3. This one
By the next cooling, the carbide 2 is cooled to about 600 to 700 ° C.
【００２１】また、この１次冷却を500 ℃以上の水蒸気
または600 ℃以上の含ＣＯ2 ガスにて行うことによっ
て、炭化物２の賦活を併せて達成する。この賦活処理に
よって炭化物の比表面積は増大するため、炭化物の吸着
機能を強化することが可能である。すなわち、炭化物２
に供給する水蒸気が500 ℃未満では、Ｃ＋H2O ＝CO＋H2
の反応が起きずに賦活処理がなされない、おそれがあ
る。同様に、炭化物２に供給する含ＣＯ2 ガスが600 ℃
未満では、Ｃ＋O2＝２COの反応が起きずに賦活処理がな
されない、おそれがある。The primary cooling is performed with steam at 500 ° C. or higher or a CO 2 -containing gas at 600 ° C. or higher, thereby simultaneously activating the carbides 2. Since the specific surface area of the carbide is increased by the activation treatment, it is possible to enhance the function of adsorbing the carbide. That is, carbide 2
If the steam supplied to the furnace is lower than 500 ° C, C + H 2 O = CO + H 2
There is a fear that the activation treatment is not performed without the reaction of Similarly, the CO 2 containing gas supplied to the carbide 2 is 600 ° C.
If it is less than 3, there is a possibility that the activation treatment is not performed without the reaction of C + O 2 = 2CO occurring.
【００２２】ここで、スクリューコンベア３内の炭化物
２に１次冷却を効率良く施すために、図２に示すよう
に、軸30に螺旋状に巻き付けた羽根31の周縁部に間隔を
置いて切り欠き31ａを設けるとともに、軸方向に羽根31
を貫通する多数の小孔31ｂを形成し、供給管４から導入
した水蒸気または含ＣＯ2 ガスを、これら切り欠き31ａ
および小孔31ｂを介して、スクリューコンベア３の全域
に満遍なく行き渡らせる。かように切り欠き31ａおよび
小孔31ｂを通路として、水蒸気または含ＣＯ2 ガスをス
クリューコンベア３内に供給すれば、搬送中の炭化物２
は水蒸気または含ＣＯ2 ガスの流れに確実に晒されるた
め、炭化物２の冷却と賦活を確実に行うことができる。Here, in order to efficiently perform the primary cooling of the carbides 2 in the screw conveyor 3, as shown in FIG. 2, the blades 31 spirally wound around the shaft 30 are cut at intervals around the periphery thereof. A notch 31a is provided, and the blade 31
Are formed, and water vapor or CO 2 -containing gas introduced from the supply pipe 4 is cut off by the cutouts 31a.
Through the small holes 31b, the screw conveyor 3 is spread evenly over the entire area. By supplying steam or CO 2 -containing gas into the screw conveyor 3 through the notch 31a and the small hole 31b as a passage, the carbide 2
Is reliably exposed to the flow of steam or a CO 2 -containing gas, so that the carbide 2 can be reliably cooled and activated.
【００２３】上記の１次冷却を経た炭化物２は、スクリ
ューコンベア３からベルトコンベア７上に切り出され、
ベルトコンベア７上を貯留ホッパ６まで搬送されるが、
このベルトコンベア７上において散水８による２次冷却
を行う。ここで、上記した１次冷却によって炭化物２の
粗熱が取り除かれているため、この２次冷却では軽微の
冷却を施せばよい。従って、多量の散水を行う必要はな
く、製品の含水率が上昇するのを回避できる。The carbide 2 having undergone the primary cooling described above is cut out from the screw conveyor 3 onto a belt conveyor 7,
It is transported on the belt conveyor 7 to the storage hopper 6,
Secondary cooling by water spray 8 is performed on the belt conveyor 7. Here, since the coarse heat of the carbide 2 has been removed by the above-described primary cooling, slight cooling may be performed in this secondary cooling. Therefore, it is not necessary to spray a large amount of water, and it is possible to avoid an increase in the water content of the product.
【００２４】なお、炭化炉１における乾留処理時に発生
する乾留ガスは、 温度調整後にスクリューコンベア３内
に導入する含ＣＯ2 ガスとして利用するか、図１に示す
ように、２次燃焼炉９において完全燃焼させる。 後者の
場合、 万一の安全を考慮して、バーナ10から高温の燃焼
ガスを吹き込むことが好ましい。そして、２次燃焼炉９
で発生した1000℃以上の高温の燃焼ガスは、 図示しない
ボイラにおいて水蒸気の形態で熱回収し、 得られた水蒸
気の温度を調整したのち、これをスクリューコンベア３
内に供給する水蒸気として用いるとよい。The carbonization gas generated during the carbonization treatment in the carbonization furnace 1 is used as CO 2 -containing gas introduced into the screw conveyor 3 after temperature adjustment, or as shown in FIG. Completely burn. In the latter case, it is preferable to blow hot combustion gas from the burner 10 in consideration of safety. And the secondary combustion furnace 9
The high-temperature combustion gas generated at 1000 ° C. or higher is recovered in the form of steam in a boiler (not shown), and the temperature of the obtained steam is adjusted.
It is good to use as steam supplied to the inside.
【００２５】[0025]
【実施例】図１に示したところに従って、炭化炉内酸素
濃度：１ vol％以下および乾留温度：600 ℃の条件を適
用して炭化物を製造した。次いで、炭化炉の出側での温
度が600 ℃の炭化物を、スクリューコンベアおよびベル
トコンベアを介して、貯留ホッパて搬送する際、スクリ
ューコンベア内に500 ℃の燃焼排ガス（含ＣＯ2 ガス）
を３〜４ｍ3 ／炭化物（kg）の流量で供給してスクリュ
ーコンベア出側の炭化物の温度を500 ℃まで低下し、さ
らにベルトコンベアでは１ｍ3 ／炭化物（kg）の流量の
散水を行って、最終的に炭化物の温度を100 ℃とした。EXAMPLE As shown in FIG. 1, a carbide was produced by applying the conditions of an oxygen concentration in a carbonization furnace of 1 vol% or less and a carbonization temperature of 600 ° C. Next, when the carbide having a temperature of 600 ° C. at the outlet side of the carbonizing furnace is transported by a storage hopper via a screw conveyor and a belt conveyor, combustion exhaust gas (including CO 2 gas) containing 500 ° C. is introduced into the screw conveyor.
Is supplied at a flow rate of 3 to 4 m 3 / carbide (kg) to lower the temperature of the carbide at the screw conveyor outlet side to 500 ° C. Further, water is supplied at a flow rate of 1 m 3 / carbide (kg) on the belt conveyor, Finally, the temperature of the carbide was set to 100 ° C.
【００２６】かくして得られた炭化物について、その性
状および成分組成について調査した。また、比較とし
て、スクリューコンベア内における燃焼排ガス（含ＣＯ
2 ガス）による冷却を行うことなく、散水のみで同様の
温度まで炭化物を冷却する、従来の処理も行い、得られ
た炭化物を同様に調査した。これらの調査結果を、表１
に示す。The properties and component composition of the carbide thus obtained were investigated. As a comparison, the combustion exhaust gas (including CO
The conventional treatment of cooling the carbide to the same temperature only by water spraying without cooling by 2 gas) was also performed, and the obtained carbide was similarly examined. Table 1 shows the results of these surveys.
Shown in
【００２７】[0027]
【表１】 [Table 1]
【００２８】[0028]
【発明の効果】この発明によれば、ごみ固形燃料を乾留
して得られる炭化物を冷却する際、水蒸気または含ＣＯ
2 ガスによって１次冷却を行ったのち、通常の散水によ
る冷却を行うため、散水による冷却の比率が抑えられて
炭化物の含水率の大幅な増加が回避されるから、高品質
の炭化物を製造することができる。また、炭化物の１次
冷却に所定温度の水蒸気または含ＣＯ2 ガスを用いるた
め、この１次冷却過程で炭化物の賦活を併せて行うこと
ができ、とりわけ活性炭としての機能に優れる炭化物の
提供が可能になる。According to the present invention, when cooling a carbide obtained by carbonizing refuse solid fuel, steam or CO-containing
After performing primary cooling with two gases, cooling by normal watering is performed, so that the cooling rate by watering is suppressed and a large increase in the water content of carbides is avoided, so that high-quality carbide is produced. be able to. In addition, since steam or CO 2 containing gas at a predetermined temperature is used for the primary cooling of the carbide, it is possible to simultaneously activate the carbide in the primary cooling process, and it is possible to provide a carbide excellent in function as activated carbon. become.
【図１】 この発明で用いる炭化物の製造装置を示す図
である。FIG. 1 is a diagram showing an apparatus for producing carbide used in the present invention.
【図２】 この発明の製造装置に適用するスクリューコ
ンベアの構造を示す図である。FIG. 2 is a diagram showing a structure of a screw conveyor applied to the manufacturing apparatus of the present invention.
１ 炭化炉 ２ 炭化物 ３ スクリューコンベア ４ 供給管 ５ ごみ固形燃料 ６ 貯留ホッパ ７ ベルトコンベア ８ 散水 DESCRIPTION OF SYMBOLS 1 Carbonization furnace 2 Carbide 3 Screw conveyor 4 Supply pipe 5 Solid waste 6 Storage hopper 7 Belt conveyor 8 Watering
───────────────────────────────────────────────────── フロントページの続き (72)発明者 山田 純夫 東京都千代田区内幸町２丁目２番３号 川 崎製鉄株式会社内 Ｆターム(参考） 4D004 AA01 AA46 AB07 BA03 BA10 CA04 CA07 CA14 CA26 CA32 CA42 CB04 CB09 CB34 CB45 CB46 CC01 CC03 DA03 DA06 DA10 4H012 HA06 4H015 AA01 AB01 BA13 BB02 BB03 CB01 ────────────────────────────────────────────────── ─── Continuing on the front page (72) Inventor Sumio Yamada 2-3-2 Uchisaiwai-cho, Chiyoda-ku, Tokyo F-term in Kawasaki Steel Corporation (reference) 4D004 AA01 AA46 AB07 BA03 BA10 CA04 CA07 CA14 CA26 CA32 CA42 CB04 CB09 CB34 CB45 CB46 CC01 CC03 DA03 DA06 DA10 4H012 HA06 4H015 AA01 AB01 BA13 BB02 BB03 CB01
Claims (6)
の形状に加工された、ごみ固形燃料を乾留して炭化物と
し、次いで該炭化物を500 ℃以上の温度の水蒸気にて冷
却したのち、散水冷却を行うことを特徴とするごみ固形
燃料を原料とした炭化物の製造方法。Claims 1. A refuse solid fuel, which has been processed into a predetermined shape through crushing, drying, and forming of refuse, is carbonized by carbonization of the refuse solid fuel, and then the char is cooled with steam at a temperature of 500 ° C. or more, and then watered. A method for producing a carbide using refuse solid fuel as a raw material, characterized by cooling.
を、炭化物の温度が600 ℃以下になるまで行うことを特
徴とするごみ固形燃料を原料とした炭化物の製造方法。2. The method according to claim 1, wherein cooling with steam is performed until the temperature of the carbide becomes 600 ° C. or less.
の形状に加工された、ごみ固形燃料を乾留して炭化物と
し、次いで該炭化物を600 ℃以上の温度の含ＣＯ 2 ガス
にて冷却したのち、散水冷却を行うことを特徴とするご
み固形燃料を原料とした炭化物の製造方法。3. Predetermined after crushing, drying and forming of garbage
The solid fuel processed in the shape of
And then converting the carbide to CO-containing at a temperature of 600 ° C. or higher. Two gas
After cooling at, water spray cooling is performed.
A method for producing carbide using solid fuel as raw material.
冷却を、炭化物の温度が700 ℃以下になるまで行うこと
を特徴とするごみ固形燃料を原料とした炭化物の製造方
法。4. The method according to claim 3, wherein cooling with the CO 2 -containing gas is performed until the temperature of the carbide becomes 700 ° C. or less.
スがごみ固形燃料を乾留する炭化炉からの排ガスである
ことを特徴とするごみ固形燃料を原料とした炭化物の製
造方法。5. The method according to claim 3, wherein the CO 2 -containing gas is an exhaust gas from a carbonization furnace for carbonizing the refuse solid fuel.
留された炭化物を搬送するスクリューコンベアを配置
し、該スクリューコンベアの経路に水蒸気または含ＣＯ
2 ガスの吹き込み手段を有することを特徴とする炭化物
の製造装置。6. A screw conveyor for transporting carbides carbonized in the carbonization furnace is disposed on the outlet side of the internal combustion type carbonization furnace, and steam or CO-containing water is fed through the screw conveyor.
An apparatus for producing carbide, characterized by having two gas blowing means.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000223333A JP2002035729A (en) | 2000-07-25 | 2000-07-25 | Method for producing carbide made from refuse derived fuel as raw material and apparatus therefor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000223333A JP2002035729A (en) | 2000-07-25 | 2000-07-25 | Method for producing carbide made from refuse derived fuel as raw material and apparatus therefor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2002035729A true JP2002035729A (en) | 2002-02-05 |
Family
ID=18717445
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2000223333A Pending JP2002035729A (en) | 2000-07-25 | 2000-07-25 | Method for producing carbide made from refuse derived fuel as raw material and apparatus therefor |
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| Country | Link |
|---|---|
| JP (1) | JP2002035729A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007307460A (en) * | 2006-05-17 | 2007-11-29 | Oguma Tekkosho:Kk | Method of cooling molding-solidified product and conveyer apparatus for it |
| JP6317020B1 (en) * | 2017-08-30 | 2018-04-25 | 株式会社神鋼環境ソリューション | Carbide manufacturing equipment |
| CN116688714A (en) * | 2023-06-07 | 2023-09-05 | 贵州绿色产业技术研究院 | System and method for continuous capture of solid amine carbon |
-
2000
- 2000-07-25 JP JP2000223333A patent/JP2002035729A/en active Pending
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007307460A (en) * | 2006-05-17 | 2007-11-29 | Oguma Tekkosho:Kk | Method of cooling molding-solidified product and conveyer apparatus for it |
| JP4612901B2 (en) * | 2006-05-17 | 2011-01-12 | 株式会社小熊鉄工所 | Molded solid product cooling method and conveyor apparatus thereof |
| JP6317020B1 (en) * | 2017-08-30 | 2018-04-25 | 株式会社神鋼環境ソリューション | Carbide manufacturing equipment |
| JP2019043987A (en) * | 2017-08-30 | 2019-03-22 | 株式会社神鋼環境ソリューション | Carbide production facility |
| CN116688714A (en) * | 2023-06-07 | 2023-09-05 | 贵州绿色产业技术研究院 | System and method for continuous capture of solid amine carbon |
| CN116688714B (en) * | 2023-06-07 | 2024-03-22 | 贵州绿色产业技术研究院 | System and method for continuous capture of solid amine carbon |
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