焦油蒸餾工段的初步設(shè)計(jì)開題報(bào)告

　　篇一：年產(chǎn)19萬(wàn)噸煤焦油工廠處理蒸餾工段的初步設(shè)計(jì)

　　河北聯(lián)合大學(xué)輕工學(xué)院

　　QINGGONG COLLEGE, HEBEI UNITED UNIVERSITY

　　畢業(yè)設(shè)計(jì)說(shuō)明書

　　設(shè)計(jì)題目：19萬(wàn)t/a煤焦油工廠處理蒸餾工段的初步設(shè)計(jì)

　　學(xué)生姓名：

　　學(xué) 號(hào)：

　　專業(yè)班級(jí)：

　　學(xué) 部：

　　指導(dǎo)教師：

　　摘  要

　　本設(shè)計(jì)為19萬(wàn)t/a焦油加工廠焦油蒸餾工段的初步設(shè)計(jì)。重點(diǎn)介紹了蒸餾工藝，通過(guò)對(duì)現(xiàn)有工藝比較，選用了國(guó)內(nèi)應(yīng)用較多且比較成熟的常壓兩塔式焦油蒸餾工藝。首先對(duì)主要設(shè)備進(jìn)行了物料衡算和熱量衡算以及設(shè)計(jì)計(jì)算及設(shè)備選型，確定了塔徑和塔高，并對(duì)塔板進(jìn)行設(shè)計(jì)計(jì)算和流體力學(xué)校核；對(duì)餾分塔進(jìn)行了機(jī)械設(shè)計(jì)和強(qiáng)度校核；最后給出非工藝條件。并用Auto-CAD繪制了帶控制點(diǎn)的工藝流程圖，精餾塔結(jié)構(gòu)圖，車間布置圖。

　　本設(shè)計(jì)的主要設(shè)備有：圓筒式管式爐350萬(wàn)千卡/小時(shí)，一段蒸發(fā)器的直徑DN=1600mm、二段蒸發(fā)器直徑DN=2400mm、餾分塔直徑DN=1800mm，塔高H=28000mm，塔板數(shù)為47，蒽塔DN=1800mm，塔板數(shù)為21，塔高H=17000mm,一段冷凝冷卻器的換熱面積是72m2，餾分塔冷凝冷卻器的換熱面積是296 m2，蒽油浸沒(méi)式冷卻器的.換熱面積是12m2等。

　　關(guān)鍵詞: 煤焦油；焦油蒸餾；餾分塔

　　Abstract

　　This design is the preliminary design of the section of 190000 t/a tar distillation in tar processing factory and mainly introduces the distillation process.According to comparing the existing process, chosing the domestic application of more and more mature tar distillation tower is two columns continuous distillation of coal tar. First of all, do the material balance and heat balance calculation，design calculation and equipment selection for he main equipment, and determine the diameter and height of the tower, and do the tower board calculation and  check design of fluid mechanics；distillation tower were mechanically designed and strengthly checked；finally，the process conditions；distillate tower mechanical design and The strength check; Finally, non-process conditions.By Auto-CAD,drawing piping and instrument diagram，the distillation column chart and workshop layout.

　　The results of the design of the main equipment is as follows.Cylindrical tube type furnace is 3.5 million kcal/h, the diameter of evaporator is 1600mm, the diameter of two sections of evaporator is 2400mm, and the diameter of fractions tower is 1800mm, whose height is 28000mm, the number of whose plate is 47, and the diameter of anthraquinone tower is 1800mm, the number of whose tower plate is 21 and whose height is 17000mm, and the cooler area of a condensation heat and the limonene condensation heat are respectively 72m2 and 296m2,and the heat transfer area of anthracene oil submerged type cooler is 12m2 etc.

　　Keywords: coal tar;tar distillation; fractions tower

　　目  錄

　　摘  要.....................................................................................................................I Abstract ............................................................................................................... II

　　前言 ........................................................................................................................ 1

　　1 文獻(xiàn)綜述 ............................................................................................................ 2

　　1.1我國(guó)煤焦油加工工業(yè)的現(xiàn)狀 .................................................................. 2

　　1.2煤焦油蒸餾工藝分類 .............................................................................. 3

　　1.2.1按工藝操作 ................................................................................... 3

　　1.2.2按操作壓力 ................................................................................... 4

　　1.2.3焦油蒸餾新工藝 ........................................................................... 6

　　1.3煤焦油加工的環(huán)保、節(jié)能及裝備水平 .................................................. 7

　　1.4發(fā)展前景 .................................................................................................. 8

　　2 工藝方案的確定及主要設(shè)備選擇 .................................................................... 9

　　2.1 工藝流程確定 ......................................................................................... 9

　　2.2 主要設(shè)備選型 ......................................................................................... 9

　　3工藝計(jì)算 ........................................................................................................... 10

　　3.1物料衡算 ................................................................................................. 10

　　3.1.1整個(gè)流程的物料衡算 ................................................................... 10

　　3.1.2主要設(shè)備的物料衡算 ................................................................. 11

　　3.2主要設(shè)備計(jì)算 ........................................................................................ 12

　　3.2.1管式加熱爐 ................................................................................... 12

　　3.2.2一段蒸發(fā)器 ................................................................................. 14

　　3.2.3二段蒸發(fā)器 ................................................................................. 15

　　3.2.4蒽塔 ............................................................................................. 15

　　3.2.5餾分塔 ......................................................................................... 17

　　3.2.6一段輕油冷凝冷卻器 ................................................................. 19

　　3.2.7餾分塔輕油冷凝冷卻器 ............................................................. 20

　　3.2.8浸沒(méi)式冷卻器（切萘洗量混餾分） ......................................... 21

　　3.3餾分塔塔板的工藝計(jì)算 ........................................................................ 22

　　3.3.1 塔徑 ............................................................................................ 22

　　3.3.2 塔高 ............................................................................................ 23

　　3.3.3圓泡罩塔盤的設(shè)計(jì) ..................................................................... 23

　　3.3.4板面布置 ..................................................................................... 24

　　3.3.5塔板壓降 ..................................................................................... 26

　　3.3.6液冷情況 ..................................................................................... 28

　　3.3.7鼓泡層高度hf ............................................................................. 28

　　3.3.8排空時(shí)間T ................................................................................. 28

　　3.4蒽塔塔板的工藝計(jì)算 ............................................................................. 29

　　3.4.1塔徑 ............................................................................................. 30

　　3.4.2圓泡罩塔盤的設(shè)計(jì) ..................................................................... 30

　　3.4.3板面布置 ..................................................................................... 31

　　3.4.4塔板壓降 ..................................................................................... 33

　　3.4.5液泛情況 ..................................................................................... 35

　　3.4.6鼓度泡層高h(yuǎn)f ............................................................................. 35

　　3.4.7排空時(shí)間T ................................................................................. 35

　　3.5容器附件 ................................................................................................ 36

　　3.5.1人孔和手孔 ................................................................................. 36

　　3.5.2視鏡 ............................................................................................. 36

　　3.5.3液面計(jì) ......................................................................................... 36

　　3.5.4接管 ............................................................................................. 37

　　3.5.5法蘭 ............................................................................................. 37

　　3.6 主要設(shè)備機(jī)械設(shè)計(jì)和強(qiáng)度校核 ........................................................... 37

　　3.6.1筒體和封頭壁厚 ......................................................................... 38

　　3.6.2塔設(shè)備載重計(jì)算 ......................................................................... 38

　　3.6.3風(fēng)載荷與風(fēng)彎矩計(jì)算 ................................................................. 41

　　3.6.4地震彎矩計(jì)算 ............................................................................. 43

　　3.6.5各種載荷引起的軸向應(yīng)力 ......................................................... 45

　　3.6.6 塔體最大組合軸向拉應(yīng)力校核 ................................................ 48

　　3.6.7 塔體水壓時(shí)應(yīng)力及吊裝時(shí)應(yīng)力校核 ........................................ 49

　　3.6.8吊裝時(shí)應(yīng)力校核校核 ................................................................. 51

　　3.6.9基礎(chǔ)環(huán)設(shè)計(jì) ................................................................................. 51

　　3.6.8地腳螺栓計(jì)算 ............................................................................. 53

　　4.非工藝條件設(shè)計(jì) .............................................................................................. 55

　　4.1防火防爆等級(jí) ........................................................................................ 55

　　4.2采暖通風(fēng) ................................................................................................ 55

　　4.3給水排水 ................................................................................................ 55

　　4.4供氣 ........................................................................................................ 56

　　4.5設(shè)備維修 ................................................................................................ 56

　　4.6電力 ........................................................................................................ 57

　　4.7土建 ........................................................................................................ 57

　　結(jié)論 ...................................................................................................................... 58

　　參考文獻(xiàn) .............................................................................................................. 59

　　謝  辭 .................................................................................................................. 61

　　篇二：開題報(bào)告焦油蒸餾

　　篇三：黑龍江科技大學(xué)本科畢業(yè)設(shè)計(jì)開題報(bào)告

　　本科畢業(yè)設(shè)計(jì)開題報(bào)告

　　題 目：10萬(wàn)噸／年焦油蒸餾工段的初步設(shè)計(jì)

　　院 （系）：  環(huán)境與化工學(xué)院

　　班 級(jí)：

　　姓 名：

　　學(xué) 號(hào)：

　　指導(dǎo)教師：

　　教師職稱：  教授

　　2015年3月

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