TWI761775B - Method for recycling waste foundry sand - Google Patents

Method for recycling waste foundry sand Download PDF

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TWI761775B
TWI761775B TW109106649A TW109106649A TWI761775B TW I761775 B TWI761775 B TW I761775B TW 109106649 A TW109106649 A TW 109106649A TW 109106649 A TW109106649 A TW 109106649A TW I761775 B TWI761775 B TW I761775B
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ceramsite
foundry sand
waste
waste foundry
sand
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TW109106649A
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TW202133956A (en
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陳長照
劉懿賢
賴姿婷
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明春窯業股份有限公司
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    • 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
    • Y02P40/60Production of ceramic materials or ceramic elements, e.g. substitution of clay or shale by alternative raw materials, e.g. ashes

Abstract

The invention relates to a method for recycling waste foundry sand and applying it to a ceramsite lightweight aggregate production system. The focus of his method is to use foundry waste sand as an auxiliary raw material for the production of ceramsite and mix it with the main raw material of natural clay, such as the Shimen reservoir silt. Then through the production process of ceramsite granulation and rotary kiln roasting. Manufacture of lightweight aggregate with high strength structure. In this production process, iron-containing components such as Fe2O3 and FeO in the waste foundry sand are used as fluxes and expansion agents in the ceramsite roasting process. The ceramsite produced by this method is more energy-saving, lightweight, heat-insulating and earthquake-resistant. It can be further widely used in green building materials, agricultural horticultural media materials, water purification filter materials and other fields. Achieving the purpose of a sustainable circular economy.

Description

廢鑄砂資源化處理方法 Waste foundry sand resource treatment method

本發明係有關一種將廢鑄砂資源化處理方法,其特徵在於,將廢鑄砂與淤泥黏土進行混合後,經製粒及焙燒製成陶粒。 The invention relates to a method for recycling waste foundry sand, which is characterized in that after mixing waste foundry sand and silt clay, granulation and roasting are performed to prepare ceramsite.

一般而言,廢鑄砂的定義為:金屬基本工業、金屬製品製造業或機械設備製造修配業在鑄造製程中所產生之廢棄鑄砂與集塵設備中所收集之鑄砂粉末物質,其主要成分為二氧化矽(SiO2)、氧化鋁(Al2O3)及氧化鐵(Fe2O3)等。依據環保署規定之「公告應回收或再利用廢棄物代碼」,廢鑄砂屬於可回收再利用廢棄物(R-1201)。 Generally speaking, waste foundry sand is defined as: waste foundry sand produced in the foundry process of the metal basic industry, metal product manufacturing industry or machinery and equipment manufacturing repair industry and the foundry sand powder collected in dust collection equipment. The components are silicon dioxide (SiO 2 ), aluminum oxide (Al 2 O 3 ) and iron oxide (Fe 2 O 3 ). According to the "Notification of Waste Codes for Recycling or Reuse" stipulated by the Environmental Protection Agency, waste foundry sand is a recyclable waste (R-1201).

按,環境工程學會、經濟部工業局及環保署的資料統計,我國近年來平均每年之廢鑄砂產量約為150萬噸。而目前主要的資源再利用化管道如大地工程的掩埋覆土、路基材料、建築填材;土木材料中的混凝土填充材、水泥添配料;農業產品的肥料添配劑等。但由於過往常被資源再利用化之管道雖多,但目前仍無法有效消化逐年增加的廢鑄砂產量。 According to statistics from the Environmental Engineering Society, the Industrial Bureau of the Ministry of Economic Affairs and the Environmental Protection Agency, the average annual output of waste casting sand in my country in recent years is about 1.5 million tons. At present, the main resource reuse pipelines are buried soil, roadbed materials, and building fillers for earth engineering; concrete fillers and cement additives in civil materials; fertilizer additives for agricultural products, etc. However, although there are many pipelines for resource reuse in the past, it is still unable to effectively digest the output of waste casting sand which increases year by year.

故,據上述廢鑄砂去化管道及目前去化之瓶頸,本發明人 則試將廢鑄砂作為陶粒原料的添配料,除增加廢鑄砂的去化管道外,透過摻配廢鑄砂後的原料性質轉變,以更綠能環保的方式,進行陶粒的生產與改良。 Therefore, according to the above-mentioned waste casting sand decontamination pipeline and the current bottleneck of decontamination, the inventors of the present invention Then try to use waste foundry sand as an additive for ceramsite raw materials. In addition to increasing the decontamination pipeline of waste foundry sand, the production of ceramsite is carried out in a greener and more environmentally friendly way by changing the properties of raw materials after blending waste foundry sand. and improvement.

造成陶粒的生成機制原理,歷經數十年來的研究,可由以下幾個觀點進行切入: After decades of research on the mechanism of the formation mechanism of ceramsite, the following viewpoints can be considered:

物理的三相變化:陶粒的焙燒製成有兩大必要構成因素,其一陶粒在高溫焙燒的過程中由固態慢慢熔融成液態,隨著焙燒時間變長,部分液態物質轉變為氣態並逐漸增加內部壓力,其二與此同時在陶粒表面之熔融態必需產生足夠黏滯度,阻礙內部氣體往外溢散。當兩必要因子同時發生時,又得以適時地進行冷卻,即形成表面緻密光滑,內部具有無數氣孔之陶粒輕質骨材。 Three-phase changes in physics: There are two necessary components for the roasting of ceramsite. One is that the ceramsite slowly melts from a solid state to a liquid state during the high-temperature roasting process. As the roasting time becomes longer, part of the liquid material turns into a gaseous state. And gradually increase the internal pressure, and at the same time, the molten state of the ceramsite surface must generate enough viscosity to prevent the internal gas from escaping. When the two necessary factors occur at the same time, they can be cooled in a timely manner, that is, a ceramsite lightweight aggregate with a dense and smooth surface and numerous pores inside is formed.

原料化學成份及其熱化學反應:根據Charles.M.Riley(1951)的研究,其受美國內政部礦物局所委託,欲由全美國各地找出可以量產陶粒之適合性原料,分析了由全美國各地採得之81件黏土及頁岩。發現其中有39件樣本會膨脹,42件樣本不會膨脹。透過礦物樣本之化學性質分析與統計歸納結果,發現氧化鋁(Al2O3)含量越高雖會提高原料之熔點,但於陶粒焙燒過程中增加陶粒之塑性並增加生成陶粒之強度。而二氧化矽(SiO2)含量越高雖會降低原料之熔點,但會降低生成陶粒之強度。而氧化亞鐵(FeO)、氧化鐵(Fe2O3)、氧化鈣(CaO)、氧化鎂(MgO)、氧化鈉(Na2O)、氧化鉀(K2O)因熔點低,除構成陶粒生成過程中的助熔劑外,亦是構成陶粒膨脹氣體的主要成分。 Chemical composition of raw materials and their thermochemical reactions: According to the research of Charles.M.Riley (1951), who was commissioned by the Bureau of Minerals of the US Department of the Interior to find suitable raw materials for mass production of ceramsite from all over the United States, analyzed the 81 pieces of clay and shale from all over the United States. Thirty-nine of the samples were found to swell and 42 of them did not. Through the analysis of chemical properties of mineral samples and the results of statistical summary, it is found that although the higher content of alumina (Al 2 O 3 ) will increase the melting point of the raw material, it will increase the plasticity of the ceramsite and the strength of the generated ceramsite during the calcination process. . The higher the content of silicon dioxide (SiO 2 ), the lower the melting point of the raw material, but the lower the strength of the generated ceramsite. While ferrous oxide (FeO), iron oxide (Fe 2 O 3 ), calcium oxide (CaO), magnesium oxide (MgO), sodium oxide (Na 2 O), potassium oxide (K 2 O) have low melting points, in addition to the composition In addition to the flux in the process of ceramsite formation, it is also the main component of the expanding gas of ceramsite.

礦物學結理的熱變化:一般礦物原料在高溫焙燒過程中, 若溫度超過礦物熔點時,因熱脫羥基作用,使礦物由原本穩定的結晶結構發生一系列的礦物相轉變而產生新的結晶構造。由過去的文獻中已知,陶粒燒成主要原料大多為黏土礦物。 Thermal changes of mineralogy structure: During the high temperature roasting process of general mineral raw materials, If the temperature exceeds the melting point of the mineral, due to thermal dehydroxylation, the mineral will undergo a series of mineral phase transformations from the original stable crystal structure to generate a new crystal structure. It is known from the past literature that the main raw materials for ceramsite firing are mostly clay minerals.

不論是廢鑄砂或是淤泥黏土,均屬我國亟待處理之可再利用資源,故本發明之動機係以淤泥黏土為主要原料,廢鑄砂為副原料,一併將其資源化再利用生產成陶粒產品後,應用於營建(含結構用與非結構用之水泥混凝土骨材原料)、園藝(土壤機介質原料)及淨水(濾材原料),使其再利用資源可納入永續使用循環外,透過生產燃料效能的改善,亦可有效降低燃料使用量,達到節能減碳效果。 Whether it is waste foundry sand or silt clay, it is a reusable resource that needs to be dealt with urgently in our country. Therefore, the motivation of the present invention is to use silt clay as the main raw material and waste foundry sand as the auxiliary raw material, and recycle them into resources for production. After the ceramsite product is formed, it can be used in construction (including structural and non-structural cement concrete aggregate raw materials), gardening (soil machine medium raw material) and water purification (filter material raw material), so that the reused resources can be included in sustainable use In addition to the cycle, through the improvement of the production fuel efficiency, the fuel consumption can also be effectively reduced, and the effect of energy saving and carbon reduction can be achieved.

本發明之主要目的在於提供一種廢鑄砂資源化處理方法,可有效將廢鑄砂與淤泥黏土進行最佳化添配,除可將兩大再利用資源納入永續經濟循環外,本系統亦可有效降低生產陶粒時的焙燒溫度,藉以達到節能減碳效果。 The main purpose of the present invention is to provide a method for treating waste foundry sand as a resource, which can effectively optimize the blending of waste foundry sand and silt clay. It can effectively reduce the roasting temperature when producing ceramsite, so as to achieve the effect of energy saving and carbon reduction.

因此,為達本發明之目的,本發明提供一種廢鑄砂資源化處理方法,包含以下步驟: Therefore, in order to achieve the purpose of the present invention, the present invention provides a method for recycling waste foundry sand, comprising the following steps:

廢鑄砂的成分分析:廢鑄砂進廠前,須先進行其元素成分、含量分析及含水量測定;乾燥、磁選與粉磨:將進廠後的廢鑄砂,置入於旋轉乾燥窯中乾燥,並以電磁鐵將廢鑄砂中的磁性金屬成分進行分離去除,再進行粉磨並透過篩網進行過篩,來確保廢鑄砂粒徑小於150μm;加水攪拌:依成分分析之結果,按比例混合淤泥黏土與廢鑄砂後,加水進 行均勻攪拌;生粒料製粒:混合後再經擠壓製粒、滾圓和良篩後得生粒料;陶粒迴轉窯焙燒:生粒料透過陶粒迴轉窯之預熱段將生粒料中水分去除後,再透過陶粒迴轉窯之焙燒段,以900至1,200℃高溫焙燒將生粒料焙燒成陶粒成品。 Composition analysis of waste foundry sand: Before the waste foundry sand enters the factory, its element composition, content analysis and moisture content must be measured; drying, magnetic separation and grinding: the waste foundry sand after entering the factory is placed in a rotary drying kiln Medium drying, and electromagnets are used to separate and remove the magnetic metal components in the waste casting sand, and then grind and sieve through a screen to ensure that the particle size of the waste casting sand is less than 150μm; adding water and stirring: according to the results of component analysis , after mixing the silt clay and waste casting sand in proportion, add water into the Stirring uniformly; granulation of raw granules: after mixing, the raw granules are obtained by extrusion granulation, spheronization and fine sieving; calcined in a ceramsite rotary kiln: the raw granules are passed through the preheating section of the ceramsite rotary kiln. After the water is removed, the raw granules are calcined into finished ceramsite products through the calcining section of the ceramsite rotary kiln at a high temperature of 900 to 1,200°C.

藉由上述步驟將廢鑄砂作為礦物添加料生產陶粒,確實具有下列優點,其詳述如下: Using waste foundry sand as a mineral additive to produce ceramsite through the above steps does have the following advantages, which are detailed as follows:

1.符合廢棄資源再利用並將其納入永續經濟循環之精神。 1. In line with the spirit of recycling waste resources and incorporating them into a sustainable economic cycle.

2.減少燃料用量(添加廢鑄砂之陶粒約降25℃的燒成溫度),降低燃料成本外,亦有效提升能源效率,達到節能減碳之環保精神。 2. Reducing the amount of fuel (the sintering temperature of ceramsite after adding waste casting sand is reduced by about 25°C), which not only reduces the fuel cost, but also effectively improves the energy efficiency and achieves the environmental protection spirit of energy saving and carbon reduction.

3.添加廢鑄砂後可有效提高陶粒之連通孔隙,使其具有較高之濾水性,擴大其產品被應用之領域範圍,如園藝、淨水等領域上之使用。 3. After adding waste foundry sand, it can effectively improve the connected pores of ceramsite, make it have higher drainage, and expand the scope of application of its products, such as gardening, water purification and other fields.

4.添加廢鑄砂後之陶粒不僅符合綠建材之理念與相關規定,更可提高其原料端及產品端的附加價值。 4. The ceramsite after adding waste casting sand not only conforms to the concept and relevant regulations of green building materials, but also can improve the added value of its raw materials and products.

S1:廢鑄砂的成分分析 S1: Composition analysis of waste foundry sand

S2:乾燥、磁選與粉磨 S2: Drying, Magnetic Separation and Grinding

S3:加水攪拌 S3: add water and stir

S4:生粒料製粒 S4: Granulation of raw pellets

S5:陶粒迴轉窯焙燒 S5: Roasting in ceramsite rotary kiln

圖1 為本發明之廢鑄砂資源化處理方法的步驟流程圖。 FIG. 1 is a flow chart of the steps of the method for recycling waste foundry sand according to the present invention.

本發明包括下列步驟之任意組合,實施方式如下範例所示: The present invention includes any combination of the following steps, and the embodiments are shown in the following examples:

製作陶粒之步驟流程請參考圖1,包含以下步驟: Please refer to Figure 1 for the process of making ceramsite, including the following steps:

廢鑄砂的成分分析步驟S1: Component analysis step S1 of waste foundry sand:

廢鑄砂會隨著不同的金屬基本工業、金屬製品製造業或機械設備製造修配業,在不同的鑄造程序、熔煉過程及集塵設備方式不同,造成其成分有所不同。故每批廢鑄砂進廠前,均須先以X-射線螢光分析儀(X-ray Fluorescence,XRF)等方式進行廢鑄砂中的二氧化矽(SiO2)、三氧化二鋁(Al2O3)、氧化鐵(Fe2O3)等元素之成分及含量分析,並以烘箱進行廢鑄砂中含水量之測定,本發明對一廢鑄砂樣本進行檢測,其成分分析數據如表1 所示:

Figure 109106649-A0305-02-0007-1
The composition of waste foundry sand will vary with different basic metal industries, metal product manufacturing or machinery equipment manufacturing and repairing industries, different casting procedures, smelting processes and different dust collection equipment methods. Therefore, before each batch of waste foundry sand enters the factory, X-ray fluorescence analyzer (X-ray Fluorescence, XRF) must be used to analyze the silicon dioxide (SiO 2 ), aluminum oxide (Al2O3) in the waste foundry sand. The composition and content of elements such as Al 2 O 3 ), iron oxide (Fe 2 O 3 ) and other elements are analyzed, and the water content in the waste casting sand is measured by an oven. As shown in Table 1:
Figure 109106649-A0305-02-0007-1

乾燥、磁選、粉磨步驟S2: Drying, magnetic separation, grinding step S2:

將進廠後的廢鑄砂,置入於旋轉乾燥窯中進行乾燥,而旋轉乾燥窯之熱源於乾、濕季時有所不同。乾季以鼓風機抽取產線上之餘廢熱進入旋轉乾燥窯內,進行廢鑄砂之乾燥;濕季則透過旋轉乾燥窯之窯頭所附設燃燒設備及窯尾的抽氣設備,以明火方式進行廢鑄砂之乾燥。完成乾燥後之廢鑄砂透過電磁鐵將其中的磁性金屬成分去除,再透過粉磨機進行粉磨,完成粉磨後的廢鑄砂以篩網進行過篩,來確保其粒徑小於150μm。 The waste casting sand after entering the factory is placed in a rotary drying kiln for drying, and the heat of the rotary drying kiln originates from the dry and wet seasons. In the dry season, a blower is used to extract the waste heat from the production line into the rotary drying kiln to dry the waste casting sand; in the wet season, the waste casting is carried out by an open flame through the combustion equipment attached to the kiln head of the rotary drying kiln and the exhaust equipment at the kiln tail. Sand drying. After drying, the waste casting sand is removed by electromagnets to remove the magnetic metal components in it, and then it is ground by a pulverizer.

加水攪拌步驟S3: Adding water and stirring step S3:

廢鑄砂經前述步驟處理後,以皮帶機搭配計量器,使廢鑄 砂與淤泥黏土進行比例摻配混合後,再使用雙軸混煉攪拌機進行混拌,同時添加適當水分,使其達到適合製粒的土壤塑性條件。 After the waste casting sand has been processed in the above steps, a belt conveyor is used with a meter to make the waste casting sand After the sand and silt clay are mixed in proportion, they are mixed with a double-shaft mixing mixer, and at the same time, appropriate water is added to make the soil plastic conditions suitable for granulation.

摻配混合比例則依據廢鑄砂及黏土檢測後之成分分析數據進行調整,以本發明所取得一淤泥黏土樣本,其成分分析數據,如表2 所示:

Figure 109106649-A0305-02-0008-2
The blending ratio is adjusted according to the component analysis data after the detection of waste foundry sand and clay. The component analysis data of a silt clay sample obtained by the present invention are shown in Table 2:
Figure 109106649-A0305-02-0008-2

以本發明所取用成分如表1 所示之廢鑄砂5~30%(樣本A)及成分如表2 所示之黏土(樣本B)70~95%進行摻配混合,該混合物其二氧化矽(SiO2)約佔50~80%、氧化鋁(Al2O3)含量約佔10~25%、助熔成份的鹼土金屬氧化物(CaO+MgO)及鹼金屬氧化物(Na2O+K2O)加總含量占5~25%。 5~30% of the waste foundry sand (sample A) with the composition shown in Table 1 and 70~95% of the clay (sample B) with the composition shown in Table 2 are used for blending and mixing. Silicon oxide (SiO 2 ) accounts for about 50~80%, alumina (Al 2 O 3 ) content accounts for about 10~25%, and the flux components are alkaline earth metal oxides (CaO+MgO) and alkali metal oxides (Na 2 ) . The total content of O+K 2 O) accounts for 5~25%.

生粒料製粒步驟S4: Raw pellet granulation step S4:

該拌合後的混合物經對輥製粒機進行生粒料的擠壓製粒、並以滾圓機進行整圓得生粒料。 The mixed mixture is subjected to extrusion granulation of raw granules by a counter-roll granulator, and rounded by a spheronizer to obtain raw granules.

陶粒迴轉窯焙燒步驟S5: Ceramsite rotary kiln roasting step S5:

該生粒料需先經過陶粒迴轉窯之預熱段將水分去除,防止高溫焙燒過程中因水分迅速蒸發造成燒裂,後經過陶粒窯之焙燒段,以900~1,200℃高溫焙燒將生粒料焙燒製成陶粒成品,再通過冷卻機進行冷卻,來防止陶粒成品因迅速冷卻所造成冷裂影響強度,最後經滾篩機篩 分,以利進行分級與後續品管。 The raw material needs to pass through the preheating section of the ceramsite rotary kiln to remove the moisture to prevent the cracking caused by the rapid evaporation of water during the high-temperature roasting process. The pellets are roasted into finished ceramsite products, which are then cooled by a cooling machine to prevent the cold cracking of the finished ceramsite products from affecting the strength due to rapid cooling. points to facilitate grading and subsequent quality control.

藉由上述步驟,本發明之實施方式確實能達到所預期之功效,又其所揭露之製程及製品,不僅未曾見諸於同類技術領域中,亦未曾公開於申請前,以上僅以實例說明本發明之構成樣態,然並非用以對本發明欲保護之範疇加以限制,基於本實施方式之修飾或變更而完成之創作,亦被視為包括於本發明的權力範疇內。 Through the above steps, the embodiment of the present invention can indeed achieve the expected effect, and the disclosed manufacturing process and products have not been seen in similar technical fields, nor have they been disclosed before the application. The above is only an example to illustrate the present invention. The composition of the invention is not intended to limit the scope of protection of the present invention, and creations based on modifications or alterations of this embodiment are also deemed to be included in the scope of the rights of the present invention.

Claims (1)

一種廢鑄砂資源化處理方法,包括下列步驟之任意組合:廢鑄砂的成分分析步驟S1:該步驟採用X-射線螢光分析儀(X-ray Fluorescence,XRF)方式進行廢鑄砂的化學及礦物成分含量分析、以及採用烘箱進行廢鑄砂之含水量測定;乾燥、磁選與粉磨步驟S2:該步驟之乾燥程序採用旋轉乾燥窯進行乾燥;該步驟之磁選程序,採用電磁鐵將廢鑄砂中的磁性金屬成分進行分離去除;該步驟之粉磨程序,採用粉磨機進行粉磨,並採用篩網進行過篩確保廢鑄砂之粒徑小於150μm;加水攪拌步驟S3:該步驟採用雙軸混煉攪拌機進行,取用廢鑄砂5~30%及淤泥黏土70~95%,同時加水均勻攪拌得一混合物;生粒料製粒步驟S4:該步驟採用對輥製粒機進行生粒料之製粒,由混合物製粒後得生粒料,並採用滾圓篩進行整圓並篩除碎泥團後進入S5步驟,篩除之碎泥團將以輸送帶送回重複S3及S4步驟;陶粒迴轉窯焙燒步驟S5:該步驟先通過陶粒迴轉窯之預熱段將生粒料之水分去除後,再經過陶粒迴轉窯之焙燒段的高溫焙燒與冷卻機之冷卻,將生粒料焙燒製成陶粒成品,陶粒於陶粒迴轉窯之預熱段及焙燒段之停留時間,採用轉速控制在每分鐘30至80轉之間,陶粒迴轉窯採用燃燒器控制其火焰溫度、火焰形狀,藉以調控陶粒焙燒時的之溫度維持在900至1,200℃。 A method for recycling waste foundry sand, comprising any combination of the following steps: component analysis of the waste foundry sand Step S1: in this step, an X-ray fluorescence analyzer (X-ray Fluorescence, XRF) is used to perform chemical analysis of the waste foundry sand and mineral composition content analysis, and use an oven to measure the water content of the waste foundry sand; drying, magnetic separation and grinding step S2: the drying process of this step uses a rotary drying kiln for drying; the magnetic separation process of this step uses an electromagnet to The magnetic metal components in the casting sand are separated and removed; in the grinding process of this step, a pulverizer is used for grinding, and a screen is used for sieving to ensure that the particle size of the waste casting sand is less than 150 μm; adding water and stirring step S3: this step Use a twin-shaft mixing mixer, take 5~30% of waste foundry sand and 70~95% of silt clay, and add water at the same time to evenly stir to obtain a mixture; raw material granulation step S4: this step is carried out with a pair of roll granulators. For the granulation of raw granules, the raw granules are obtained after granulating the mixture, and the spheronizing screen is used to complete the circle and screen out the crushed mud mass and then enter the step S5. Step S4; calcining step S5 in the ceramsite rotary kiln: this step first removes the moisture of the raw granules through the preheating section of the ceramsite rotary kiln, and then passes through the high-temperature roasting and cooling of the cooling machine in the calcining section of the ceramsite rotary kiln, The raw granules are roasted to make ceramsite finished products. The residence time of ceramsite in the preheating section and the roasting section of the ceramsite rotary kiln is controlled by the rotation speed between 30 and 80 revolutions per minute, and the ceramsite rotary kiln is controlled by a burner. Its flame temperature and flame shape are used to control the temperature of ceramsite calcination to maintain at 900 to 1,200 ℃.
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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TW200508170A (en) * 2003-08-22 2005-03-01 Tung-Hsuan Lu Material of controlled low strength materials, CLSM
CN1944602A (en) * 2006-10-30 2007-04-11 四川雷鸣生物环保工程有限公司 Method for one-step producing biomassfuel, biological haydite and active carbon using high wet mixed city garbage as raw material
TW201827358A (en) * 2017-01-26 2018-08-01 潤泰精密材料股份有限公司 Method for preparing porous material

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TW200508170A (en) * 2003-08-22 2005-03-01 Tung-Hsuan Lu Material of controlled low strength materials, CLSM
CN1944602A (en) * 2006-10-30 2007-04-11 四川雷鸣生物环保工程有限公司 Method for one-step producing biomassfuel, biological haydite and active carbon using high wet mixed city garbage as raw material
TW201827358A (en) * 2017-01-26 2018-08-01 潤泰精密材料股份有限公司 Method for preparing porous material

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