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編號(hào)
無(wú)錫太湖學(xué)院
畢業(yè)設(shè)計(jì)（論文）
相關(guān)資料
題目： 滾筒干燥器設(shè)計(jì)
信機(jī) 系 機(jī)械工程及自動(dòng)化專(zhuān)業(yè)
學(xué) 號(hào)： 0923011
學(xué)生姓名： 呂春輝
指導(dǎo)教師： 戴寧 （職稱：副教授 ）
（職稱： ）
2013年5月25日
目 錄
一、畢業(yè)設(shè)計(jì)（論文）開(kāi)題報(bào)告
二、畢業(yè)設(shè)計(jì)（論文）外文資料翻譯及原文
三、學(xué)生“畢業(yè)論文（論文）計(jì)劃、進(jìn)度、檢查及落實(shí)表”
四、實(shí)習(xí)鑒定表
無(wú)錫太湖學(xué)院
畢業(yè)設(shè)計(jì)（論文）
開(kāi)題報(bào)告
題目： 滾筒干燥器設(shè)計(jì)
信機(jī) 系 機(jī)械工程及自動(dòng)化 專(zhuān)業(yè)
學(xué) 號(hào)： 0923011
學(xué)生姓名： 呂春輝
指導(dǎo)教師： 戴寧 （職稱：副教授 ）
（職稱： ）
2012年11月25日
課題來(lái)源
工程實(shí)踐類(lèi)的自擬課題
科學(xué)依據(jù)（包括課題的科學(xué)意義；國(guó)內(nèi)外研究概況、水平和發(fā)展趨勢(shì)；應(yīng)用前景等）
（1）課題科學(xué)意義
干燥技術(shù)的應(yīng)用，在我國(guó)具有十分悠久的歷史，聞名于世的造紙技術(shù)就有干燥技術(shù)的應(yīng)用。干燥設(shè)備廣泛應(yīng)用于化工、食品、糧油、飼料等工業(yè)。中國(guó)的現(xiàn)代干燥技術(shù)是從20 世紀(jì)50年代逐漸發(fā)展起來(lái)的，迄今對(duì)于常用的干燥設(shè)備如氣流干燥、噴霧干燥、流化床干燥、旋轉(zhuǎn)閃蒸干燥、紅外干燥、微波干燥、冷凍干燥等設(shè)備，我國(guó)均能生產(chǎn)供應(yīng)市場(chǎng)。對(duì)于一些較新型的干燥技術(shù)如沖擊干燥、對(duì)撞流干燥、過(guò)熱干燥、脈動(dòng)燃燒干燥、熱泵干燥等也都已開(kāi)發(fā)研究，有的已工業(yè)化應(yīng)用。我國(guó)的現(xiàn)代干燥技術(shù)取得的成績(jī)是我國(guó)相關(guān)科研人員和企業(yè)界共同努力的結(jié)果，雖然取得了不少可喜的成果，但是企業(yè)間的競(jìng)爭(zhēng)尚不規(guī)范阻礙了干燥技術(shù)的健康發(fā)展，很多成果尚未能轉(zhuǎn)化為生產(chǎn)力使企業(yè)的產(chǎn)品得不到更新。
（2）國(guó)內(nèi)外研究概況及發(fā)展前景
干燥也是一個(gè)能耗較大的單元操作，直接決定著產(chǎn)品的質(zhì)量，特別是高性能材料的生產(chǎn)，對(duì)干燥操作有著更高的要求。針對(duì)這些問(wèn)題，近些年來(lái)，干燥技術(shù)領(lǐng)域出現(xiàn)了一些創(chuàng)新成果。為了節(jié)能以及生產(chǎn)附加值高的產(chǎn)品、解決干燥過(guò)程中出現(xiàn)的問(wèn)題需要結(jié)合現(xiàn)存的各種有效的干燥技術(shù)，或者研究開(kāi)發(fā)特殊的干燥技術(shù)和新型的干燥設(shè)備同時(shí)也需要強(qiáng)化干燥過(guò)程中的智能化控制。在油脂制取的原料干燥上目前我國(guó)此類(lèi)干燥設(shè)備大部分是采用對(duì)流干燥技術(shù),主要使用滾筒烘干機(jī)、流化床烘干機(jī)和塔式干燥機(jī)。 簡(jiǎn)而言之，目前干燥技術(shù)發(fā)展的總趨勢(shì)為:
a.干燥設(shè)備研制上向?qū)I(yè)化、大型化、系列化和自動(dòng)化發(fā)展。
b.強(qiáng)化干燥過(guò)程。
c.采用新的干燥方法和組合干燥方法。
d.降低干燥過(guò)程中能量的消耗。
e.閉路循環(huán)干燥流程的開(kāi)發(fā)和應(yīng)用。
f.消除干燥過(guò)程造成的公害問(wèn)題。
研究?jī)?nèi)容
① 熟悉滾筒干燥器的主要原理和結(jié)構(gòu)。
② 熟悉干燥過(guò)程的基本計(jì)算；
③ 熟練進(jìn)行滾筒干燥器的結(jié)構(gòu)設(shè)計(jì)；
④ 掌握ＣＡＤ的使用方法；
⑤ 能夠熟練使用ＵＧ進(jìn)行三維的畫(huà)圖設(shè)計(jì)。
擬采取的研究方法、技術(shù)路線、實(shí)驗(yàn)方案及可行性分析
（1）實(shí)驗(yàn)方案
對(duì)滾筒干燥機(jī)進(jìn)行設(shè)計(jì)，結(jié)構(gòu)合理、布局正確，能夠正常運(yùn)行。
（2）研究方法
① 用ＣＡＤ進(jìn)行二維畫(huà)圖，對(duì)滾筒干燥器的結(jié)構(gòu)有全面的了解。
② 對(duì)滾筒干燥機(jī)進(jìn)行計(jì)算與結(jié)構(gòu)設(shè)計(jì)，使其滿足工作要求。
研究計(jì)劃及預(yù)期成果
研究計(jì)劃：
2012年10月12日-2012年12月31日：按照任務(wù)書(shū)要求查閱論文相關(guān)參考資料，完成畢業(yè)設(shè)計(jì)開(kāi)題報(bào)告書(shū)。
2013年1月1日-2013年1月27日：學(xué)習(xí)并翻譯一篇與畢業(yè)設(shè)計(jì)相關(guān)的英文材料。
2013年1月28日-2013年3月3日：畢業(yè)實(shí)習(xí)。
2013年3月4日-2013年3月17日：滾筒干燥器的主要參數(shù)計(jì)算與確定。
2013年3月18日-2013年4月14日：滾筒干燥器總體結(jié)構(gòu)設(shè)計(jì)。
2013年4月15日-2013年4月28日：零件圖及三維畫(huà)圖設(shè)計(jì)。
2013年4月29日-2013年5月21日：畢業(yè)論文撰寫(xiě)和修改工作。
預(yù)期成果：
滾筒干燥器可以正常運(yùn)行，完成人們所需的成品。
特色或創(chuàng)新之處
① 設(shè)備傳熱效率高、傳熱均勻。
② 設(shè)備結(jié)構(gòu)簡(jiǎn)單、易操作。
已具備的條件和尚需解決的問(wèn)題
① 設(shè)計(jì)方案思路已經(jīng)明確，已經(jīng)具備機(jī)械設(shè)計(jì)能力和干燥方面的知識(shí)。
② 進(jìn)行結(jié)構(gòu)設(shè)計(jì)的能力尚需加強(qiáng)。
指導(dǎo)教師意見(jiàn)
指導(dǎo)教師簽名：
年 月 日
教研室（學(xué)科組、研究所）意見(jiàn)
教研室主任簽名：
年 月 日
系意見(jiàn)
主管領(lǐng)導(dǎo)簽名：
年 月 日
英文原文
Drying Technology
There are three main types of gas-suspension dryers:
· Spray dryers, to convert a liquid solution or suspension to a dry, free-flowing powder
· Fluid-bed dryers, used to dry wet filter cake, or for pastes and sludges with dry product recirculation
· Flash dryers, for a relatively dry, crumbly, non-sticky feed
The type of dryer chosen for any given application depends on both the feed properties and product requirements. Important feed properties are the moisture content, solids, viscosity, and density, as well as any volatile, flammable, or toxic components. Dried product specifications may include average particle size and particle size distribution, density, moisture content, and residual volatiles or solvents. Powder characteristics can be controlled and powder properties maintained constant through continuous operation.
Spray Drying
Spray drying is a three-step drying process involving both particle formation and drying. (1) The process begins with the atomization of a liquid feed into a spray of fine droplets. (2) Then a heated gas stream suspends the droplets, evaporating the liquid and leaving the solids in essentially their original size and shape. (3) Finally, the dried powder is separated from the gas stream and collected. Spent drying gas is either treated and exhausted to the atmosphere or recirculated to the system. These three steps are accomplished by three components: the atomizer, the disperser, and the drying chamber.
The selection and operation of the atomizer is of extreme importance in achieving an optimum operation and production of top-quality powders. There are four main types of atomization:
· Centrifugal atomization, the most common, uses a rotating wheel or disc to break the liquid stream into droplets. The rotational speed determines the mean particle size, while the particle size distribution about the mean remains fairly constant in a system. Centrifugal atomizers are available in a large variety of sizes, from laboratory scale to very large commercial units.
· Hydraulic pressure-nozzle atomization forces pressurized fluid through an orifice. Multiple nozzles are used to increase capacity. The particle size depends on the pressure drop across the orifice, so that the orifice size determines the capacity of the system. This type of atomization is simpler than centrifugal, but cannot be controlled as well. It is not suitable for abrasive materials, or materials that tend to plug the orifices.
· Two-fluid pneumatic atomization uses nozzles, as well, but introduces a second fluid, usually compressed air, into the liquid stream to atomize it. This type of atomization has the advantage of relatively low pressures and velocities and a shorter required drying path. It is most often used in small-scale equipment, laboratory or pilot size.
· Sonic atomization, not yet widely used, passes a liquid over a surface vibrated at ultrasonic frequencies. It can produce very fine droplets at low flow rates. Current limitations are capacity and the range of different product that can be atomized.
After atomization, a disperser brings the heated gas into contact with the droplets. The disperser must accomplish three things: mix the gas with the droplets, begin the drying process, and determine the flow paths through the drying chamber. The drying gas may be heated directly by combustion of natural gas, propane, or fuel oil, or indirectly using shell-and-tube or finned heat exchangers. Electric heaters may be used in small dryers. Industrial radial fans move the heated gas through the system.
The drying chamber must be sized to allow adequate contact time for evaporation of all of the liquid to produce a dry powder product. Factors that impact the drying time include the temperature difference between the droplets and the drying gas, and their flow rates. The exact shape of the chamber depends on the drying characteristics and product specifications, but most are cylindrical with a cone-shaped lower section to facilitate collection of the product.
Finally, proper configuration of the atomizer, disperser, and drying chamber is essential for complete drying and to avoid the deposit of wet material on the interior surfaces of the dryer. Designs may use co-current, counter-current, or mixed flow patterns.
The powder is separated from the drying gas at the bottom of the chamber. Most often, the gas exits through an outlet duct in the center of the cone. Heavier or coarser particles will be separated at this point, dropping into the cone to be collected through an air lock. Then either cyclones or fabric filters (or both) remove the remaining powder from the exit gas. In systems producing a very fine powder, most of the collection takes place at this point.
Fluid-Bed Drying
Fluid-bed drying is a process in which a gas is forced upward through a bed of moist particles to achieve a fluidized state. The particles are suspended in the gas stream and dry as they flow along with the gas. Fluid beds can be either cylindrical or rectangular. There are two basic types of fluid-bed designs:
· Plug flow fluid beds are used for feeds that are directly fluidizable. Baffles in the bed limit mixing in the horizontal direction to maintain plug flow. This type of bed is ideal for removal of bound volatiles or for heating and cooling. The volatile content and temperature vary uniformly as the solids pass through the bed. Baffle design depends on the shape and size of the bed, with spiral or radial baffles used in circular beds and straight baffles in rectangular.
· Back-mixed fluid beds are used for feeds that cannot be fluidized in their original state, but become fluidizable after a short time in the dryer. The feed is distributed over the bed surface, designed to allow total solids mixing. Product temperature and moisture are uniform across the fluidized layer. Heating surfaces may be immersed in the fluidized layer to improve thermal efficiency and performance.
A combination system uses a back-mixed fluid bed to reduce the moisture level of the wet feed, followed by a plug-flow section to achieve final specifications. This type of arrangement is quite common.
The advantages of fluidized-bed drying are: relatively long residence times allow high heat-transfer coefficients between the particles and the gas; the ability to closely control product temperature makes fluidized beds ideal for processing temperature-sensitive solids; and they have the highest thermal efficiency of any gas-suspension drying system.
Disadvantages are: they can process only a limited range of materials; product particles are relatively large; and there may be difficulty processing needle- or platelet-shaped particles.
Flash Drying
Flash drying forces drying gas through a heater and upward through a duct or flash tube. The high-velocity gas stream instantly suspends the feed, which enters just after the heater, and carries it to the collection equipment, usually cyclones or bag collectors.
Flash dryers are the simplest gas-suspension dryers, and require the least space. Residence time within the dryer is very short, usually less than 3 seconds. Particles must be quite small, and the best feed is reasonably dry, crumbly, and not sticky. There are several ways to obtain the required feed qualities:
· A cage mill may be used to break up the feed into the required small particles.
· If the feed is too wet or pasty, dry solids may be backmixed to create the proper consistency.
· An agitated design, using a high-speed disintegrating rotor, will keep all particles moving. This design is shorter and larger in diameter than a flash tube, creating a very compact system.
Hybrid Dryers
There are a number of hydrid systems used in applications where a single system cannot handle the requirements of both the feed and product. The most common are:
· Fluidized spray dryers (FSD?) combine spray with fluid bed drying to produce agglomerated products. The top of the system is a spray dryer, atomizing the liquid and contacting it with heated gas. Additional heated gas is introduced at the bottom to create a fluidized bed portion of the drying chamber. This type of dryer will produce a dustless, free-flowing agglomerated product. It is ideal for products that must dissolve easily, e.g. food colors, dyestuffs, pigments, and some agricultural chemicals.
· A flash dryer may be used to remove surface moisture, followed by a fluid bed for removal of bound moisture.
Niro Dryers
The MOBILE MINOR? is a laboratory-scale spray dryer known for its flexibility and different levels of control systems. It is used to dry small quantities of solutions, suspensions, and emulsions into representative powder samples. Test results provide important information for selecting the design and technical specification of a given drying project.
The PRODUCTION MINOR? is a larger spray dryer that can be used for pilot testing or small-scale production. It has a choice of atomizers, heating systems, and powder discharge.
The Fluidized Spray Dryer (FSD?) was invented and patented by Niro in the early 1980s. It combines fluidization and spray-drying technologies to dry a wide variety of products, including many that cannot be dried using conventional equipment. Advantages include easy control of the size and structure of the particles, making it ideal for agglomerated products, and low powder temperatures for thermally sensitive materials. It is also very energy efficient.
中文譯文
干燥技術(shù)
主要有三種氣體懸浮烘干:
噴霧干燥器,把液體溶液或懸浮于干燥,自由流動(dòng)的粉末
流化床干燥機(jī),用干,濕濾餅,或漿和污泥干產(chǎn)品再循環(huán)
閃蒸干燥機(jī),在相當(dāng)干燥,松軟,非飼料粘粘
該型干燥器選擇任何特定應(yīng)用取決于雙方的飼料性能和產(chǎn)品的要求. 重要飼料性能是水分含量,固形物,粘度,密度,以及任何揮發(fā)性,易燃或有毒成分. 木片產(chǎn)品規(guī)格可能包括平均粒度分布,密度,含水率,殘留揮發(fā)或溶劑. 粉末特性可控制粉末特性保持不變,通過(guò)連續(xù)運(yùn)行.
噴霧干燥.
噴霧干燥是一個(gè)三步走的干燥過(guò)程中,涉及兩種粒子形成和干燥. ( 1 )進(jìn)程始于霧化的液體飼料成噴霧霧滴. ( 2 ) ,然后加熱氣流暫時(shí)飛沫 96.3%的液體和離開(kāi)固體基本上是原來(lái)的大小和形狀. ( 3 )最后,干粉分離氣流和收集. 用干燥氣體要么是治療和精疲力竭的氣氛或循環(huán)使用該系統(tǒng). 這三個(gè)步驟是由三部分組成:霧化,分散,而干燥室.
選擇和操作的噴霧器,是極端重要性,實(shí)現(xiàn)最佳的操作和生產(chǎn)頂級(jí)質(zhì)量 粉末. 主要有4種霧化:
離心霧化,最常見(jiàn)的,用一個(gè)旋轉(zhuǎn)輪或盤(pán)打破液體流成液滴. 轉(zhuǎn)速確定的平均粒徑, 而粒度分布大約平均維持在相當(dāng)穩(wěn)定的系統(tǒng). 離心式霧化器可有多種尺寸,從實(shí)驗(yàn)室規(guī)模比較大的商業(yè)單位. 液壓噴嘴霧化勢(shì)力加壓流體通過(guò)一個(gè)小孔. 多噴頭用來(lái)增加容量. 顆粒大小取決于壓降過(guò)孔板, 使孔大小決定了系統(tǒng)的容量. 這種霧化簡(jiǎn)單得多離心,但無(wú)法控制等. 它是不適合研磨材料,或材料,往往堵塞孔口. 雙流體氣動(dòng)霧化噴嘴的用途,以及如何引進(jìn),但第二液,通常壓縮空氣 成液體流霧化. 這種霧化的優(yōu)點(diǎn)在于較低的壓力和速度,縮短干燥所需的路徑. 這是最常用的小型設(shè)備,實(shí)驗(yàn)室或中試規(guī)模. 聲波霧化,尚未廣泛使用,在經(jīng)過(guò)了超過(guò)液體表面振搗,在超聲波的頻率. 它可以產(chǎn)生非常細(xì)微的動(dòng)作,在低流率. 電流限制能力,以及各種不同的產(chǎn)品,可霧化.
霧化后,使分散的熾熱氣體接觸到液滴. 分散必須完成三件事:混合氣體與霧滴,從干燥過(guò)程中, 并確定流路徑通過(guò)干燥室. 干燥氣體,可直接加熱燃燒天然氣,丙烷或燃油 或間接使用殼管式或翅片式換熱器. 電加熱器,可用于小型烘干機(jī). 工業(yè)徑向球迷提出了激烈的天然氣通過(guò)該系統(tǒng). 烘干室必須大小以便有充裕的時(shí)間接觸蒸發(fā)所有的液體產(chǎn)生 一個(gè)干粉產(chǎn)品. 因素的影響,干燥時(shí)間,包括溫差的霧滴和干燥氣體. 而其流率. 確切庭取決于干燥特性及產(chǎn)品規(guī)格, 但大多數(shù)是圓柱與錐形下段,以方便收集的產(chǎn)品. 最后,妥善配置的噴霧器,播種機(jī), 和干燥室必須徹底干燥,以避免存款濕材料的內(nèi)表面 在吹干. 設(shè)計(jì)可利用順流,逆流或混合流模式. 粉末分離的干燥氣室底部. 在多數(shù)情況下,出口氣體通過(guò)一個(gè)插座導(dǎo)管中心的錐. 較重或粗顆粒將會(huì)分開(kāi),在這一點(diǎn)上, 墜入錐可通過(guò)收集空鎖. 然后要么旋風(fēng)或織物過(guò)濾器(或兩者)來(lái)清除殘留的粉末從出口氣. 在系統(tǒng)產(chǎn)生非常微細(xì)粉末,大部分的收集發(fā)生在這一點(diǎn).
流化床干燥
流化床干燥過(guò)程中的氣體被迫通過(guò)向上一床濕顆粒實(shí)現(xiàn) 沸騰狀態(tài). 這些微粒懸浮在氣流和干燥,因?yàn)樗麄兞麟S氣. 流化床可分為圓柱形或長(zhǎng)方形. 有兩個(gè)基本類(lèi)型的流化床設(shè)計(jì):
堵塞流病床被用作飼料,是直接發(fā)霉. 擋板床攪拌限制在水平方向上保持堵塞水流. 這種床是理想的搬遷勢(shì)必?fù)]發(fā)或加熱和冷卻. 揮發(fā)量與溫度變化一致的固體通過(guò)床底下. 擋板的設(shè)計(jì)取決于形狀和尺寸的床, 螺旋或徑向隔板采用圓形床和直擋板的長(zhǎng)方形. 返混流化床用作飼料,不能流于原始狀態(tài), 但成為發(fā)霉后,在很短的時(shí)間干燥. 飼料派發(fā)超過(guò)床面,旨在讓總固體混合. 產(chǎn)品的溫度和濕度都是一刀切流化床層. 受熱面,可沉浸在流態(tài)化層,以提高熱效率和業(yè)績(jī).
組合系統(tǒng)采用返混流化床,以減少水分含量的濕飼料 其次是一個(gè)插件流斷面,以達(dá)到最終規(guī)格. 這種安排是司空見(jiàn)慣. 優(yōu)點(diǎn)流化床干燥如下: 較長(zhǎng)的停留時(shí)間,讓高傳熱系數(shù)與粒子間的氣體; 能密切控制產(chǎn)品溫度使得流化床理想的加工溫度敏感固體; 他們有最高的熱效率氣體懸浮干燥系統(tǒng). 缺點(diǎn)是:它們能過(guò)程只是一個(gè)范圍有限的材料; 產(chǎn)品顆粒較大; 并有可能難以處理針頭或血小板形顆粒.
速干
速干勢(shì)力干燥氣體通過(guò)一個(gè)加熱器,向上通過(guò)導(dǎo)管或閃光燈管. 高速氣流瞬間停止飼料,其中大部分進(jìn)入剛剛加熱器 縹緲,它的采集設(shè)備,通常旋風(fēng)或袋收藏. 閃蒸干燥機(jī)是最簡(jiǎn)單的氣體懸浮烘干機(jī),并要求最少的空間. 居留時(shí)間內(nèi)干燥,是非常短,通常小于3秒. 粒子必須相當(dāng)小,而最好的飼料是合理的干燥,松軟,不發(fā)粘. 有幾種方法,以取得所需的飼料品質(zhì):
籠子軋機(jī)可用于擊破飼料成所需的小顆粒. 如果飼料過(guò)于潮濕或糊狀,干物質(zhì)可backmixed創(chuàng)造適當(dāng)?shù)囊恢滦? 激動(dòng)的設(shè)計(jì),采用高速粉碎轉(zhuǎn)子,會(huì)讓所有粒子. 這個(gè)設(shè)計(jì)是較短時(shí)間和較大的直徑比閃光燈管,創(chuàng)造一個(gè)非常緊湊的系統(tǒng).
混合式干燥機(jī)
有一些氫化系統(tǒng)在應(yīng)用中,一個(gè)單一的系統(tǒng),不能處理的要求,既 飼料和產(chǎn)品. 最常見(jiàn)的有:
流化床噴霧干燥器(消防?)結(jié)合噴霧流化床干燥制粒生產(chǎn)的產(chǎn)品. 頂級(jí)的系統(tǒng)是一個(gè)噴霧干燥機(jī),霧化液接觸,并與熾熱氣體. 新增天然氣加熱介紹,在底部形成流化床部分的干燥室. 這種烘干機(jī)將產(chǎn)生一個(gè)無(wú)塵,自由流動(dòng)的壓塊產(chǎn)品. 它是理想的產(chǎn)品,必須解散容易,例如: 食用色素,染料,顏料,以及一些農(nóng)業(yè)化學(xué)品. 一個(gè)旋轉(zhuǎn)閃蒸干燥機(jī),可用于去除表面水分,然后由流化床去除一定水分.
Niro干燥
移動(dòng)輕微?是一個(gè)實(shí)驗(yàn)室規(guī)模噴霧干燥機(jī)已知的靈活性和不同層次的控制系統(tǒng). 它是用來(lái)干少量溶液,懸浮,乳液為代表的粉末樣本. 測(cè)試結(jié)果提供了重要信息,為選擇設(shè)計(jì)和技術(shù)規(guī)格,某一干燥工程. 生產(chǎn)小型?是一個(gè)較大型噴霧干燥機(jī),可用于試驗(yàn)或小規(guī)模生產(chǎn). 它可以選擇霧化器,暖氣系統(tǒng),粉塵排放. 04-0357噴霧干燥機(jī)(消防?) ,發(fā)明和專(zhuān)利niro在八十年代初期. 它集流和噴霧干燥技術(shù),干燥的多種產(chǎn)品, 其中有許多是不能曬干使用常規(guī)設(shè)備. 優(yōu)點(diǎn)包括易于控制的規(guī)模和結(jié)構(gòu)的粒子,使之適合壓塊產(chǎn)品 低氣溫粉熱敏感材料. 這也是很有效的能源.