Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP2862408B2 - Method for producing hydraulic product - Google Patents
[go: Go Back, main page]

JP2862408B2 - Method for producing hydraulic product - Google Patents

Method for producing hydraulic product

Info

Publication number
JP2862408B2
JP2862408B2 JP3168007A JP16800791A JP2862408B2 JP 2862408 B2 JP2862408 B2 JP 2862408B2 JP 3168007 A JP3168007 A JP 3168007A JP 16800791 A JP16800791 A JP 16800791A JP 2862408 B2 JP2862408 B2 JP 2862408B2
Authority
JP
Japan
Prior art keywords
sio
product
coal ash
high temperature
producing
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
JP3168007A
Other languages
Japanese (ja)
Other versions
JPH0517184A (en
Inventor
信之 池田
智規 小山
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP3168007A priority Critical patent/JP2862408B2/en
Publication of JPH0517184A publication Critical patent/JPH0517184A/en
Application granted granted Critical
Publication of JP2862408B2 publication Critical patent/JP2862408B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B7/00Hydraulic cements
    • C04B7/24Cements from oil shales, residues or waste other than slag
    • C04B7/26Cements from oil shales, residues or waste other than slag from raw materials containing flue dust, i.e. fly ash
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P40/00Technologies relating to the processing of minerals
    • Y02P40/10Production of cement, e.g. improving or optimising the production methods; Cement grinding

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Organic Chemistry (AREA)
  • Processing Of Solid Wastes (AREA)
  • Curing Cements, Concrete, And Artificial Stone (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は建築土木工事等に適用さ
れる水硬性生成物、例えばセメントの製造方法に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a hydraulic product, for example, cement, which is applied to construction and civil engineering.

【0002】[0002]

【従来の技術】従来のセメントの製造方法としては、原
料に硅石、石灰石等を使用して、機械的粉砕による方法
が行なわれている。
2. Description of the Related Art As a conventional method for producing cement, a method of mechanically pulverizing silica, limestone or the like as a raw material has been used.

【0003】[0003]

【発明が解決しようとする課題】従来技術には、原料
(硅石、粘土)を購入し、粉砕を行なわなければならな
いので、コストが高くなるという問題点がある。
The prior art has a problem in that the raw materials (silica, clay) must be purchased and pulverized, which increases the cost.

【0004】一方、産業用石炭焚ボイラにおいては、燃
焼後の石炭灰を埋め立て処分を行なっているが、用地確
保及び環境問題等で年々、困難になってきている。
[0004] On the other hand, in industrial coal-fired boilers, burnt coal ash is landfilled and disposed, but it is becoming more and more difficult year by year due to land securing and environmental problems.

【0005】本発明は上記技術水準に鑑み、不要成分で
ある石炭灰を利用して、セメントのような水硬性生成物
を製造する方法を提供しようとするものである。
The present invention has been made in view of the above-mentioned state of the art, and aims to provide a method for producing a hydraulic product such as cement using coal ash which is an unnecessary component.

【0006】[0006]

【課題を解決するための手段】本発明は石炭灰を高温条
件下で燃焼させてSiO2 を気化させ、該高温下の気化
SiO2 に微細なCaO又はCaCO3 粒子を反応さ
せ、生成物を冷却後捕集することを特徴とする水硬性生
成物の製造方法である。
The present invention SUMMARY OF THE INVENTION The vaporizing SiO 2 by burning coal ash under high temperature conditions, reacting the fine CaO or CaCO 3 particles in the vaporization of SiO 2 under the high temperature, the product A method for producing a hydraulic product, which comprises collecting after cooling.

【0007】本発明において、石炭灰を高温条件下で燃
焼させてSiO2 を気化させるに当っては、酸素富化空
気を用いた燃焼炉で2300℃以上の高温状態にするこ
とが好ましい。
In the present invention, in burning coal ash under high temperature conditions to vaporize SiO 2 , it is preferable to set the temperature to 2300 ° C. or higher in a combustion furnace using oxygen-enriched air.

【0008】また、CaO又はCaCO3 粒子はその蒸
発・気化を促進するために、10μm以下の粒度にする
ことが好ましい。
The CaO or CaCO 3 particles preferably have a particle size of 10 μm or less in order to promote their evaporation and vaporization.

【0009】[0009]

【作用】高温場に投入された石炭灰はSiO2 とAl2
3 に分離し、その分離されたSiO2 は同高温場に投
入された10μm以下のCaO又はCaCo3 と化合し
て、3CaO・SiO2 (C3 Sと略記)、又は2Ca
O・SiO2 (C2 Sと略記)の水硬性組成物(ポルト
ランドセメント)になる。
[Action] Coal ash introduced into a high temperature field is SiO 2 and Al 2
O 3, and the separated SiO 2 is combined with 10 μm or less of CaO or CaCo 3 introduced into the high-temperature field to form 3CaO · SiO 2 (abbreviated as C 3 S) or 2Ca
It becomes a hydraulic composition (Portland cement) of O.SiO 2 (abbreviated as C 2 S).

【0010】この水硬性組成物でセメント成分全体の5
0%以上を占めるC3 Sは速硬性型セメントと言える。
In this hydraulic composition, the total amount of cement components is 5%.
C 3 S occupying 0% or more can be said to be a quick-setting cement.

【0011】[0011]

【実施例】本発明に係る実施例を図1によって説明す
る。酸素富化燃焼器8(以下、燃焼器という)は、上端
が排ガス管1に連通し、下端に燃焼器8の中心に向って
下方に傾斜する水冷管18と耐火材19で構成されるス
ラグタップ部4と、円筒状の水冷管3と、耐火材5等で
構成された本体と、同本体の上端近傍より石炭と酸化剤
(酸素、および空気)および石炭灰10a,10bをそ
れぞれ供給する複数個のバーナ11a,11bを有す
る。燃焼器8の下部スラグタップ部4には溶融スラグ6
が落下するように、炉中心部に排出孔2が穿設されてい
る。
An embodiment according to the present invention will be described with reference to FIG. The oxygen-enriched combustor 8 (hereinafter, referred to as a combustor) has a slag composed of a water-cooled pipe 18 having an upper end communicating with the exhaust gas pipe 1 and a lower end inclined downward toward the center of the combustor 8, and a refractory material 19. A main body composed of a tap portion 4, a cylindrical water-cooled pipe 3, a refractory material 5, and the like, and coal, an oxidizing agent (oxygen and air), and coal ash 10a and 10b are supplied from near the upper end of the main body. It has a plurality of burners 11a and 11b. The molten slag 6 is provided in the lower slag tap portion 4 of the combustor 8.
A discharge hole 2 is drilled in the center of the furnace so that the gas falls.

【0012】石炭と酸化剤および石炭灰10a,10b
は燃焼器8内で燃焼し、2300℃以上の高温となり、
石炭灰に含まれるSiO2 は気化する。気化したSiO
2 12は排ガス管1の方に流れる。そこに投入された1
0μm以下のCaO又はCaCO3 13a,13bはS
iO2 12と反応し、エーライト3CaO・SiO2
4となる。その後、冷却ガス15a,15bで冷却され
固化し、セメント16となり、図示しないバグフィルタ
等で回収される。
Coal and oxidizer and coal ash 10a, 10b
Burns in the combustor 8 and reaches a high temperature of 2300 ° C. or higher,
SiO 2 contained in coal ash is vaporized. Vaporized SiO
2 12 flows to the exhaust gas pipe 1. 1 put in there
CaO or CaCO 3 13a, 13b of 0 μm or less is S
Reacts with iO 2 12 and alite 3CaO · SiO 2 1
It becomes 4. Then, it is cooled and solidified by the cooling gas 15a, 15b to become cement 16, which is collected by a bag filter (not shown) or the like.

【0013】下部スラグタップ部4より落下したスラグ
17は図示しない水タンクにより急冷され非晶質の水砕
スラグとなり、粉砕されてコンクリート混和剤として使
用される。
The slag 17 that has fallen from the lower slag tap portion 4 is rapidly cooled by a water tank (not shown) to become amorphous granulated slag, which is crushed and used as a concrete admixture.

【0014】[0014]

【発明の効果】本発明により下記の効果が奏される。
石炭灰を使用することにより原料が安価になる。
スラグもコンクリート混和剤として使用することができ
るため、有効活用できる。 燃焼コントロールによ
り、シリカの混合比調整が可能である。 従来の粉砕
による方法より原料の粉砕、混合等が簡略化できる。
以上の効果によって製品の単価が安くなる。 石炭
灰の有効活用が計れる。
The present invention has the following effects.
The use of coal ash makes the raw material cheaper.
Since slag can also be used as a concrete admixture, it can be used effectively. By controlling the combustion, the mixing ratio of silica can be adjusted. The pulverization and mixing of the raw materials can be simplified as compared with the conventional pulverization method.
Due to the above effects, the unit price of the product is reduced. Effective utilization of coal ash can be measured.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の一実施例の説明図FIG. 1 is an explanatory diagram of an embodiment of the present invention.

フロントページの続き (58)調査した分野(Int.Cl.6,DB名) C04B 7/26 C04B 7/02Continuation of front page (58) Field surveyed (Int.Cl. 6 , DB name) C04B 7/26 C04B 7/02

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 石炭灰を高温条件下で燃焼させてSiO
2 を気化させ、該高温下の気化SiO2 に微細なCaO
又はCaCO3 粒子を反応させ、生成物を冷却後捕集す
ることを特徴とする水硬性生成物の製造方法。
1. Coal ash is burned under high temperature conditions to produce SiO
2 is vaporized, and fine CaO is added to the vaporized SiO 2 under the high temperature.
Alternatively, a method for producing a hydraulic product, comprising reacting CaCO 3 particles, collecting the product after cooling, and collecting the product.
JP3168007A 1991-07-09 1991-07-09 Method for producing hydraulic product Expired - Fee Related JP2862408B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3168007A JP2862408B2 (en) 1991-07-09 1991-07-09 Method for producing hydraulic product

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3168007A JP2862408B2 (en) 1991-07-09 1991-07-09 Method for producing hydraulic product

Publications (2)

Publication Number Publication Date
JPH0517184A JPH0517184A (en) 1993-01-26
JP2862408B2 true JP2862408B2 (en) 1999-03-03

Family

ID=15860078

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3168007A Expired - Fee Related JP2862408B2 (en) 1991-07-09 1991-07-09 Method for producing hydraulic product

Country Status (1)

Country Link
JP (1) JP2862408B2 (en)

Also Published As

Publication number Publication date
JPH0517184A (en) 1993-01-26

Similar Documents

Publication Publication Date Title
US4265671A (en) Method of utilizing fly ash from power works and refuse disposal plants in the production of cement clinkers, and a plant for carrying out said method
JP5984599B2 (en) Method for producing cement composition
WO2001030944A1 (en) Clean combustion of coal, utility of the concomitant product of the clean combustion and the product by using the concomitant product
CA2312576C (en) Combustion process applicable to the manufacture of cement
JP2862408B2 (en) Method for producing hydraulic product
CN105819717A (en) Production method of cement clinker
JP3435497B2 (en) Activated fly ash and method for producing the same
JPH0155363B2 (en)
JP3358940B2 (en) Coal ash utilization system
JP4157662B2 (en) Cement clinker and cement composition
JP7218211B2 (en) Cement manufacturing method
CN1028984C (en) Method for producing masonry cement by calcining marl in a fluidized bed boiler
JP2575963B2 (en) Manufacturing method of hydraulic material
JPH11139854A (en) Mortar / concrete admixture and mortar / concrete composition
GB1587023A (en) Clinker material including pulverised fuel ash
US4664042A (en) Method of decreasing ash fouling
JPS6053805B2 (en) Combustible sludge treatment method
JPH0910731A (en) Method for producing fine spherical molten granules from sludge incineration ash
US2271276A (en) Process for producing cement
JP2003238220A (en) Method of producing activated fly ash
JPS62158144A (en) Quicklime recovery method and equipment in lime kiln
JP2587486B2 (en) Manufacturing method of cement
JPH0422614B2 (en)
JP3217537B2 (en) Method of reforming fly ash
JPH0418913A (en) Stack gas desulfurization process

Legal Events

Date Code Title Description
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 19981110

LAPS Cancellation because of no payment of annual fees