36萬噸滑油系統(tǒng)浮頭式換熱器設(shè)計(jì)（全套含CAD圖+說明書+開題報(bào)告+翻譯）
資源目錄里展示的全都有，所見即所得。下載后全都有,請放心下載。原稿可自行編輯修改=【QQ：401339828 或11970985 有疑問可加】
畢 業(yè) 設(shè) 計(jì) (論 文)
題 目： 36萬噸滑油系統(tǒng)浮頭式換熱器
學(xué)院名稱： 機(jī)械工程學(xué)院
指導(dǎo)教師：
職 稱：
班 級：
學(xué) 號：
學(xué)生姓名：
20 年5月28日
畢業(yè)設(shè)計(jì)任務(wù)書
學(xué) 院： 機(jī)械工程學(xué)院
題 目： 36萬噸滑油系統(tǒng)浮頭式換熱器設(shè)計(jì)
設(shè)計(jì)（論文）內(nèi)容及要求：
一、 已知設(shè)計(jì)參數(shù)；
滑油流量50 /h，進(jìn)口溫度45，出口溫度40，冷卻水流量54/h，進(jìn)口溫度33，管程殼程操作壓力為0.435MPa。
冷凝器類型 浮頭式
二、設(shè)計(jì)內(nèi)容及設(shè)計(jì)工作量要求：
（1）按所給設(shè)計(jì)參數(shù)完成的浮頭式冷凝器的施工圖設(shè)計(jì)；
（2）繪制設(shè)計(jì)圖紙總計(jì)3張零號以上，其中要求手工繪圖1張壹號以上；
（3）設(shè)計(jì)說明書字?jǐn)?shù)不少于1.5萬字，并要求統(tǒng)一用A4紙打??；
（4）翻譯3千左右漢字量的與畢業(yè)設(shè)計(jì)有關(guān)的英文資料；
（5）撰寫相當(dāng)于3百漢字的英文摘要。
三、主要參考資料：
《 化工設(shè)備設(shè)計(jì)全書（換熱器）》
GB150-1998《鋼制壓力容器》
GB151-1999《管殼式換熱器》
指導(dǎo)教師： 年 月 日
南華大學(xué)本科生畢業(yè)設(shè)計(jì)（論文）開題報(bào)告
設(shè)計(jì)（論文）題目
36萬噸滑油系統(tǒng)浮頭式換熱器設(shè)計(jì)
設(shè)計(jì)（論文）題目來源
自選課題
設(shè)計(jì)（論文）題目類型
工程設(shè)計(jì)類
起止時間
2011/1/6-2011/5/31
一、 設(shè)計(jì)（論文）依據(jù)及研究意義：
本設(shè)計(jì)為浮頭式換熱器設(shè)計(jì)；設(shè)計(jì)參考的前提是常減壓裝置中的工藝條件，根據(jù)裝置工藝條件選擇具體的流量、溫度、壓力等參數(shù)。
對浮頭式換熱器的研究，將更多地激發(fā)人們對換熱器這方面問題的興趣與注意力，投資、研究和發(fā)展,其結(jié)果不僅帶來傳熱理論和裝備水平的提高,將更好地促進(jìn)工業(yè)經(jīng)濟(jì)發(fā)展,為節(jié)約能源和保護(hù)環(huán)境也會產(chǎn)生無法估量的推廣意義。
二、 設(shè)計(jì)（論文）主要研究的內(nèi)容、預(yù)期目標(biāo)：（技術(shù)方案、路線）
主要研究的內(nèi)容：
1、工藝計(jì)算
2、結(jié)構(gòu)設(shè)計(jì)
3、換熱器核算
4、筒體和封頭計(jì)算
5、換熱器零部件結(jié)構(gòu)設(shè)計(jì)（包括分層隔板、折柳板、拉桿、定距桿、防沖板、接管等）
6、換熱器機(jī)械機(jī)構(gòu)設(shè)計(jì)（包括管板、管箱、法蘭、墊片、支座等）
7、強(qiáng)度校核
預(yù)期目標(biāo)：（技術(shù)方案、路線）
浮頭式換熱器是由管箱、筒體、管板、封頭、折流板、換熱管等零部件組成，根據(jù)換熱管材料、尺寸、管數(shù)、管程壓力、管壁溫度、管程數(shù)以及殼體材料、內(nèi)徑、厚度、殼程壓力、溫度等條件下確定管板的厚度、折流板的形狀、尺寸與數(shù)量、折流板的布置情況和確定換熱器的結(jié)構(gòu)尺寸。
工藝設(shè)計(jì)——蒸發(fā)、換熱器的結(jié)構(gòu)和強(qiáng)度設(shè)計(jì)——施工圖繪制——使用說明書制訂
三、設(shè)計(jì)（論文）的研究重點(diǎn)及難點(diǎn)：
研究重點(diǎn)是結(jié)構(gòu)設(shè)計(jì)以及筒體和封頭的計(jì)算，這不僅要求我們對換熱器有一定了解，而且要有嚴(yán)密的計(jì)算能力。
研究的難點(diǎn)在于換熱器零部件結(jié)構(gòu)設(shè)計(jì)，以及換熱器機(jī)械機(jī)構(gòu)設(shè)計(jì)，這要求我們熟悉換熱器的設(shè)計(jì)制造要求，同時也是對整個專業(yè)只是的運(yùn)用。
四、 設(shè)計(jì)（論文）研究方法及步驟（進(jìn)度安排）：
研究方法：
首先閱讀大量相關(guān)文獻(xiàn)資料,教材及新聞背景資料,包括換熱器制造的原理及方法，質(zhì)量管理應(yīng)用換熱器現(xiàn)有技術(shù)水準(zhǔn),國際水平探討方面的書籍,報(bào)刊.以了解可靠性的內(nèi)容,質(zhì)量管理的概況和換熱器領(lǐng)域的基本知識體系.然后通過調(diào)研,進(jìn)一步了解企業(yè)現(xiàn)狀及需求.接下來進(jìn)行分析與設(shè)計(jì).確定數(shù)據(jù)來源的真實(shí)準(zhǔn)確.再進(jìn)行系統(tǒng)設(shè)計(jì)
步驟：（進(jìn)度安排）
１、準(zhǔn)備階段（1月10號～2月10號）．搜集有關(guān)資料，準(zhǔn)備參考資料
2、完成開題報(bào)告及論文大綱交老師批閱（2月11日～2月25日）
3、按所給設(shè)計(jì)參數(shù)完成浮頭式換熱器的結(jié)構(gòu)尺寸計(jì)算、強(qiáng)度計(jì)算校核（2月26號～4月26號）；
4、繪制設(shè)計(jì)圖紙總計(jì)3張零號以上，其中要求手工繪圖1張壹號以上（4月27號～5月10號）；
5、設(shè)計(jì)說明書字?jǐn)?shù)不少于1.5萬字，并要求統(tǒng)一用A4紙打?。?月11號～5月20號）；
6、翻譯3千左右漢字量的與畢業(yè)設(shè)計(jì)有關(guān)的英文資料；（5月21號～5月25號）
7、撰寫相當(dāng)于3百漢字的英文摘要（5月26號～5月30號）。
五、 進(jìn)行設(shè)計(jì)（論文）所需條件：
1、要有充分的資料（在圖書館查閱與浮頭式換熱器相關(guān)的書籍，進(jìn)行篩選，選出有用的信息）。
2、具備手工和電腦繪圖的能力以及相應(yīng)的壓力容器理論知識，同時還要有老師的指導(dǎo)。
六、 指導(dǎo)教師意見：
簽 名： 年 月 日
5 翻譯
5.1 英文原文
Shell-and-tube and plate heat exchanger water Comparative Analysis
Abstract: Through the closed cycle cooling water system in thewater water heat interchanger shaping, in detail elaborated the shell type and the disc heat interchanger structure performance technology economy compares, provides the reference for the water and water heat interchanger shaping.
Keyword: Heat interchanger performance comparison
From the domestic power plants have been built, for closed-cycle cooling water system of water heat exchanger two categories. is a shell and tube type heat exchangers, and the other is the plate heat exchanger. Shell heat exchanger is used in the form of heat exchanger in the plant design has been widely used, In some domestic units of the plant imports, the gas-steam combined cycle power plants and nuclear power plants are more used plate heat exchanger. Plate heat exchanger as a compact, light weight, high heat transfer efficiency, and the people are interested in growing. This paper shell - and-tube heat exchanger plate and two kinds of styles, and make selection suggestions
1. A plate and shell heat exchanger structure brief
(1) Shell type heat interchanger
Shell-and-tube heat exchanger is the former Marine Room, probation, cylinder, the water room and so on. Control the use of pumped - Bundle, which consists of around tube sheet, Baffled, the stick, distance control, Tube components. Stick with the management board, demolition of the plates using screw connection tube and tube sheet adopted inflation accelerating sealed welding. In the shell side entrance to the control of water on board-equipped to prevent the cooling water washed Tube. In order to reduce the load or to take control of the cylinder friction, with the control on the slide. Room for cleaning up the rubbish, sediment and the blockage of the tubes in the water around the room on the Cover of an inspection hole. To monitor water heat exchanger performance, in the cooling water side (except salt water side) and the cooling water side (of seawater) for the import and export are equipped with a temperature and pressure measurement, There is also supposed to exhaust and interfaces.
(2) Plate heat exchanger
plate heat exchanger consists of a set of parallel corrugated sheet metal components, Plates in the four corner have access hole, Clamping plate was in connection with an aspect of the fixed plate compactor and activities in the framework of plate and clamping bolts used to be clamping. Connecting with the board of the channel pore right, and with two heat exchange liquid external piping connected Heat plate compactor and activities flag at the top plate bearing beams below it from the bottom of the beams at the position. Plate heat itself is a specific shape surrounded by solid-tight gasket seal to prevent external leakage. and the two heat exchange liquid form by alternating current to flow through another pair of plate heat transfer between the channel. Plates of corrugated not only improves the fluid turbulence, and creating many points of contact to withstand normal operating pressure. Fluid flow, physical properties, the pressure and temperature differential decision of the plate number and size.
2 Heat interchangers design conditions
Heat exchanger design of the plant from the start to meet the greatest contribution to the various load operating conditions to take dollars, and leave enough margin to ensure heat exchanger in the maximum load and maximum inlet temperature and the largest Fouling, in the repair cycle, it was to be given the task of cooling. Domestic imported 300 MW coal-fired units as an example. Cooling equipment requirements of the cooling water inlet temperature is less than 37.5 ° C, from the cooling equipment was heating up over the cooling water temperature is about 42.8 ℃
3 Shells types and disc heat interchanger comparison
3.1 Flows the heat transfer design comparison
Shell-and-tube heat exchanger tube heat exchanger is an essential component, It tube in a fluid flowing through the tube and another providing heat transfer fluid between the surface. According to both the fluid nature of pipe materials, will be corrosive, low-quality water on the water pipe flow In addition to better water quality brine on the shell side of the tubes, such tubes only used seawater corrosion-resistant titanium tube. Meanwhile more convenient cleaning dirt diameter from the point of view of heat transfer fluid dynamics, given the use of the shell of small diameter tubes can be greater density on the surface, but most fluid in the tubes on the surface dirt layer deposition, In particular, the cooling tube poor water, silt and dirt and sea organisms exist, are likely to be formed on the wall of sediments, will enable heat transfer deterioration regular cleansing becomes necessary, tube cleaning restrictions smallest diameter of about 20 mm, Titanium Tube general, 25 mm, the right to the fluid, formed mainly by dirt wall temperature and velocity impact to be reasonable maintenance cycle, the water inside the tube velocity in two 1961 (as to allow pressure drop requirements). As general use seawater cooling water, the river, prone to causing scaling the shell - and-tube heat exchanger, Water should be equipped concentration of plastic ball cleaning device for cleaning. Plate heat exchanger in the cooling water and cooling water on both sides of the corrugated plate convection, using corrugated chevron Bellows, These corrugated plate heat transfer bias, that is adjacent to the heat plate with the same angle of inclination and direction of the bellows. Cross sectional area along the direction of flow is constant, but due to the changing direction of flow resulting flow shape change, which leads to turbulence. Heat general corrugated plate depth of 3-5 mm, the turbulent flow is about 0.1 ~ 1.0 to 1.4 ms Bellows thin plate thickness 0.6~1 mm and the adjacent cubicle to have many points of contact to withstand normal operating pressure adjacent to the boards opposite direction of the chevron trench, two grooves on the intersection point of contact formation, this can also eliminate vibration, and the promotion of the exchange of heat and turbulence at the same time, eliminate fatigue cracks as a result of the internal leakage. Chevron corrugated plate turbulent higher, high turbulence can play a full role in cleaning, can be particularly effective deposition dirt minimized, but corrugated board more points of contact, when liquid water quality poor, containing suspended solid particles, debris and weeds, etc., because of the narrow gap plate. So to the extent possible, ensure that all particles above 2 mm into the heat exchanger in the past, must strip, If the filter can effectively play a role, it is easy to plug.
3.2 Heat transfer coefficients comparison
Shell heat exchanger tube, a horizontal fluid passing through the tube wall and pipe flow of a heat transfer fluid, mutual vertical cross-flow heat transfer coefficient is generally 1000~3000 w/ (m2.k).
Plate heat exchanger, the cooling water side with the side of the cooling water flow uniformity turbulence, the two reverse fluid flow As the ripple effect caused turbulence, resulting in higher heat transfer rate, high resistance to pressure and high shear stress field. This will lead to inhibit heat transfer surface of the dirt formed. Heat transfer coefficient is generally 3500~5500 w/ (m2.k), which can save heat exchanger heat transfer area.
3. Ends difference comparison
Shell-and-tube heat exchanger temperature difference (that is, the cooling water inlet temperature and the cooling water outlet temperature difference) 5 ℃.
Plate heat exchanger due to its structural characteristics can be done to the economy as low as 1 ° C temperature difference.
3.4 Cooling water volume comparison
Shell-and-tube heat exchanger general cooling and water cooling water than a 1.2~2.5:1.
Plate heat exchanger, as two kinds of media flow with the same high heat transfer efficiency, Therefore plate heat exchanger can greatly reduce the cooling water, the general cooling water and cooling water than a 0.8~1.1 : 1, thus reducing pipe valves and pumps installed operating costs
3.5 Installments overhauls comparison
Plate heat exchanger is small in size, light weight characteristics, maintenance convenience, without lifting based maintenance facilities, Therefore, the installation occupies less. Plate heat exchanger including the artificial maintenance unit packs will be opened, using water guns and brush cleaning plates and gaskets, check plate gasket and, if necessary, replace the plate and gasket. Plate heat exchanger generally a time to clean, and whether or not the actual needs to be done. When the application of the river, poor water quality, such as cooling water, silt and dirt because of the existence, and the rapid growth of microorganisms have caused pollution and the surface plug danger. Overseas, the application of water for cooling water, cleaning high frequency, the average annual 3.3. Shell-and-tube heat exchanger tube bundle is composed of its own weight is larger volume, maintenance of the pumping required to stay out of control as long distance, it occupies more needed with the necessary lifting overhaul facilities.
Shell-and-tube heat exchanger design life-expectancy of 30 years, overhaul cycle four years, when heat exchanger leaked, (probably tubes and tube plate of tube leakage or rupture caused by the leakage) can be used to plug the pipe recovery in a short period of time Minute performance, shell - and-tube heat exchanger allows the blocking of 7% margin. For pipe cleaning may need plastic ball cleaning device for the mechanical cleaning regularly.
4 Heat interchangers in domestic power plant movement situation
My early commissioning of the 300 MW coal-fired units closed cooling water systems are chosen shell - and-tube heat exchanger water. running relatively well. In recent years, because of the continuous advancement of technology, design optimization, shell - and-tube exchangers covers water, Maintenance of large venues in the main shortcomings of the plant layout optimization more prominent, In some circulating water system for secondary cooling water circulation unit, taking into account the water cooling heat exchanger of the relatively good water quality, Impurities less pollution and the small screen structure of continuous improvement, closed cooling water systems also use plate heat exchanger.
5 Conclusion
On shell - -tube and plate heat exchanger the comparison may come to the following conclusions : Plate heat exchanger for high heat transfer efficiency, small size, light in weight dismounting, when cooling water better, It is an ideal heat exchanger equipment. But for a large number of cooling water sediment and dirt, such as the presence of water, the filters can not effectively play its role it is easy to plug, resulting in frequent cleansing affect the safe operation of the unit.
譯文：
管殼式與板式水水換熱器的比較分析
摘要：通過閉式循環(huán)冷卻水系統(tǒng)中水水換熱器的選型，詳細(xì)論述了管殼式與板式換熱器的結(jié)構(gòu)性能技術(shù)經(jīng)濟(jì)比較，為水水換熱器的選型提供參考。
關(guān)鍵詞：換熱器 性能 比較
? 從國內(nèi)已建發(fā)電廠來看，用于閉式循環(huán)冷卻水系統(tǒng)的水水換熱器有兩類，一類是管殼熱換器，另一類是板式換熱器。管殼換熱器是常用的換熱器形式，在電廠設(shè)計(jì)中已得到了廣泛的應(yīng)用，而在國內(nèi)一些進(jìn)口機(jī)組的電廠、燃?xì)庹羝?lián)合循環(huán)電廠和核電站多有采用板式換熱器。由于板式換熱器緊湊、重量輕、高傳熱效率，人們對它的興趣日益增長。本文針對管殼式及板式換熱器二種型式進(jìn)行比較，并提出選型參考意見。
1 管殼式及板式換熱器結(jié)構(gòu)簡介
（1）管殼式換熱器
? 管殼式換熱器是由前水室、管束、筒體、后水室等組成。管束采用可抽式管束，它由前后管板、折流板、拉桿、定距管、換熱管組成。拉桿與管板、拆流板采用絲扣連接，換熱管與管板采用脹接加密封焊。在殼側(cè)水入口處的管束上設(shè)置防沖板，以防止被冷卻水直接沖刷換熱管。為了減少管束裝入或抽出筒體時的摩擦力，在管束上設(shè)有滑軌。為了檢查清理室中垃圾、泥沙及管子的堵塞等，在前后水室端蓋上設(shè)有檢查孔。為了監(jiān)視水水換熱器的運(yùn)行情況，在被冷卻水側(cè)（除鹽水側(cè)）及冷卻水側(cè)（海水側(cè)）進(jìn)出口都設(shè)置溫度和壓力測點(diǎn)，此外還設(shè)有排氣和放水接口等。
（2）板式換熱器 ?
板式換熱器是由一組波紋形的平行金屬板構(gòu)成的，在板片的4個拐角處都有通道孔，板被夾緊在一個側(cè)面附有連接管的固定板和活動壓緊板的框架中，并用夾緊螺栓加以夾緊。這些連接管同板上的通道孔對中，并與熱交換的兩種液體的外部管路相連，傳熱板和活動壓緊板懸掛在頂部承載梁的下面并由底部橫梁使其對準(zhǔn)定位。
傳熱板本身是有其有特定形狀并被固緊的墊片密封，以防止外部泄漏，并把熱交換的兩種液體按逆流方式交替地流過另一對傳熱板之間的通道內(nèi)。板片上的波紋不但提高流體的湍流程度，并且形成許多接觸點(diǎn)，以承受正常的運(yùn)行壓力。流體的流量、物理性質(zhì)，壓降和溫度差決定了板片的數(shù)目和尺寸。
2 換熱器設(shè)計(jì)條件
換熱器設(shè)計(jì)應(yīng)滿足電廠從起動到最大出力時各種負(fù)荷下的運(yùn)行需要，并留有一定的裕量，保證換熱器在最大負(fù)荷、最高進(jìn)水溫度和最大污垢熱阻時，在規(guī)定的檢修周期內(nèi)，仍能完成給定的冷卻任務(wù)。
以國產(chǎn)引進(jìn)型300 MW燃煤機(jī)組為例，各冷卻設(shè)備要求冷卻水進(jìn)水溫度不大于37．5℃，從冷卻設(shè)備出來被加熱過的冷卻水最高溫度約為42．8℃.
3 管殼式及板式換熱器的比較
3．1流動傳熱設(shè)計(jì)比較
管殼式換熱器的管子是換熱器的基本構(gòu)件，它為在管內(nèi)流過一種流體和穿越管外的另一種流體之間提供傳熱面。根據(jù)兩側(cè)流體的性質(zhì)決定管子材料，將具有腐蝕性，水質(zhì)差的海水放在管內(nèi)流動，水質(zhì)較好的除鹽水放在管子外殼側(cè)，這樣管子只需采用耐海水腐蝕的鈦管，同時清洗污垢較為方便，管徑從傳熱流體力學(xué)角度考慮，在給定殼體內(nèi)使用小直徑管子，可以得到更大的表面密度，但大多數(shù)流體會在管子表面上沉積污垢層，尤其管內(nèi)冷卻水水質(zhì)較差，泥沙和污物及海生物的存在，都可能會在管壁上形成沉積物，將傳熱惡化并使定期的清洗工作成為必要，管子清洗限制管徑最小約為20 mm，鈦管一般采Φ25 mm，對給定的流體，污垢形成主要受管壁溫度和流速的影響，為得到合理的維修周期，管內(nèi)側(cè)水的流速應(yīng)在2 m／s左右（視允許壓降的要求）。由于一般冷卻水選用海水、河水等，較易引起結(jié)垢，對管殼式換熱器，應(yīng)根據(jù)水質(zhì)含沙量情況需設(shè)置膠球清洗裝置進(jìn)行定期清洗。
板式換熱器的冷卻水和被冷卻水在波紋板的兩側(cè)對流，波紋采用人字形波紋，這些傳熱板的波紋斜交，即在相鄰的傳熱板上具有傾斜角相同而方向不同的波紋。沿流動方向橫截面積是恒定的，但是由于流動方向不斷變化致使流道形狀改變，而引起湍流。一般傳熱板的波紋深度為3～5 mm，湍流區(qū)流速約為0.1～1.0 m／s，波紋板很薄，厚度為0．6～1 mm，相鄰板間要有許多接觸點(diǎn)，以承受正常的運(yùn)行壓力，相鄰的板有相反方向的人字形溝槽，兩種溝槽的交叉點(diǎn)就形成接觸點(diǎn)，這樣還可消除振動，并且在促進(jìn)湍流和熱交換的同時，消除了由于疲勞裂縫引起的內(nèi)部泄漏。人字形波紋板湍流度較高，高湍流還能充分發(fā)揮清洗作用，可以特別有效的將沉積污垢減至最小，但是波紋板的接觸點(diǎn)較多，當(dāng)液體水質(zhì)差，含有懸浮的固體顆粒、雜物和水草等時，由于板間隙很窄，所以要盡可能地保證將所有2 mm以上顆粒在進(jìn)入換熱器以前，都要過濾掉，假如濾網(wǎng)不能有效地發(fā)揮作用，就容易發(fā)生堵塞。
3．2 傳熱系數(shù)的比較
管殼體換熱器中，一種流體橫向掠過管子通過管壁與管內(nèi)流動的另一種流體換熱，彼此垂直交叉流動，其傳熱系數(shù)一般為1000～3000 w／（m2．k）。 ?
板式換熱器中，冷卻水側(cè)與被冷卻水側(cè)流動均勻湍流，兩種流體逆向流動，由于波紋的作用引起湍流，從而產(chǎn)生高傳熱率，高阻力壓降以及高切應(yīng)力場，這將導(dǎo)致抑制污垢在傳熱面上形成。其傳熱系數(shù)一般為3500～5500 w／（m2．k），由此，可節(jié)省換熱器的換熱面積。
3．3 端差比較
管殼式換熱器傳熱端差（即冷卻水進(jìn)口溫度和被冷卻水出口溫度差）為5℃左右。板式換熱器由于它的結(jié)構(gòu)特點(diǎn)可以經(jīng)濟(jì)地做到低至1℃的端差。
3．4 冷卻水量比較
管殼式換熱器一般冷卻水量和被冷卻水量之比為1．2～2．5∶1。
板式換熱器，由于2種介質(zhì)流道基本相同且傳熱效率高，因此板式換熱器可大大降低冷卻水量，一般冷卻水量和被冷卻水量之比為0．8～1．1∶1，這樣可以降低管道閥門和泵的安裝運(yùn)行費(fèi)用。
3．5 安裝檢修的比較
板式換熱器具有體積小，重量輕的特點(diǎn)，檢修方便，不需設(shè)檢修起吊設(shè)施，故安裝占地較少。板式換熱器的人工維護(hù)包括將整機(jī)折開，用噴水槍和刷子清洗板和墊片，檢查板片和墊片，如有必要，更換板片和墊片。板式換熱器一般每年要清洗1次，并且無論是否實(shí)際需要都要做。當(dāng)應(yīng)用河水、海水等水質(zhì)較差的冷卻水時，由于泥沙和污物的存在，以及微生物的快速生長有引起表面污染和堵塞的危險。在國外，應(yīng)用河水作冷卻水時，清洗頻率很高，平均每年3．3次。
管殼式換熱器是由管束組成，自身重量體積都較大，在檢修抽管時需要留出管束一樣長的距離，故占地較多，還需配備必要的起吊檢修設(shè)施。管殼式換熱器的設(shè)計(jì)壽命一般為30年，大修周期4年，當(dāng)換熱器發(fā)生泄漏時，（可能是管子與管板間的泄漏或是管子破裂引起的泄漏）可以采用堵管的辦法在短時間內(nèi)恢復(fù)工作性能，管殼式換熱器允許有7％的堵管裕量。對于管內(nèi)的清洗可以根據(jù)需要采用膠球清洗裝置進(jìn)行定期的機(jī)械清洗。
4 換熱器在國內(nèi)電廠的運(yùn)行情況
我國早期投產(chǎn)的300 MW的燃煤機(jī)組閉式冷卻水系統(tǒng)大多選用管殼式水水換熱器，運(yùn)行情況都比較好。近年來由于技術(shù)的不斷進(jìn)步，設(shè)計(jì)優(yōu)化的需要，管殼式水水換器占地面積大、檢修場地大的缺點(diǎn)在主廠房布置優(yōu)化中更顯突出，在一些循環(huán)水系統(tǒng)為二次循環(huán)冷卻水的機(jī)組中，考慮到水水換熱器的冷卻水水質(zhì)相對較好、雜質(zhì)少、污染小以及濾網(wǎng)結(jié)構(gòu)的不斷改進(jìn)，閉式冷卻水系統(tǒng)中亦有選用板式換熱器。
5 結(jié)論
通過對管殼式及板式換熱器的比較，可以得出以下結(jié)論：板式換熱器傳熱器傳熱效率高、體積小、重量輕便于拆裝，當(dāng)冷卻水水質(zhì)較好時，它是一種比較理想的換熱器設(shè)備。但是對于冷卻水中有大量泥沙、污物、水草等存在時，濾網(wǎng)又不能有效地發(fā)揮作用，很容易使其堵塞，造成頻繁地清洗，影響機(jī)組的安全運(yùn)行。
收藏