设计源文件-4.换热器结果

第一章概 换热器概 第二章换热器的选型说 外形和规 壳和台 工艺条件限 第三章换热器设计举 工艺数据汇 类型选 温度和压 传热系 尺 管径与管 排列形 管 管.................................................................................................................................折流 EDR计算结 计算结 详细结 附件1换热器设计结果一览 附件2换热器设计结果TEMA 第一章《化工设备设计全书—换热器》2003-《石油化工设备选型手册—换热器》2009-《化工工艺设计手册》2003-《压力容器安全技术监察规1990-5-《实用热物理性质手册》《钢制压力容器》GB150-《管壳式换热器》GB151-《管径选择》HG/T20570.6-《化工配管用无缝及焊接尺寸选用系列》HG20553-《石油化工企业尺寸系列》SH3405-《氨制冷装置用卧式蒸发器》JB/T7658.4-《鞍式支座》JB/T4712-备之一。换热器行业涉及暖通、压力容器、中水处理设备，化工，石油等近30多种产业，相互形成条。数据显示2010年中国换热器产业市场规模在500亿元左右，主要集中于石804040、核电常规岛核岛、风力发电机组能光伏发电、多晶硅生产等领域都需要大130、艺流中使用着大量的换热器提高这些换热器效率显然可以减少能源的消耗；压力降得范围；对、维修的要求；材料价格；使用等。流量、腐蚀性、允许压降、操作温度与压力、结垢情况和检修等要素决定选壳壁与管壁的温差超过70℃；壁温相差50~70℃。而壳流体压力大0.6MPa壳流体易结垢或腐蚀性强时不能采用固定管板式换热器综合考虑本次管壳式(又称列管式)换热器是管壳式换热器主要有壳体、管束、管板和封头等部分组成，壳体多呈圆形，装有平行管束或者螺旋管，管束两端固定于管板上。在管壳换热器内进行换热的两种流体，一种在管内流动，其行称为管一种在管外流动，其行称为壳管束的壁面即为传热面。管壳式换热4.614000w/m2.k，大大提高生产效率，更换胶条价格昂贵（胶条的更换费用大约占整个过的1/3-1/2）.主要应用于液体-液体之间的换热，行业内常称为水水换热，其换热效率在5000w/m2.K。泛。目前，由于中国新版GMP的推出，板式换热将逐渐退出食品，饮料，制药等第二章热器的选型 壳都符合设计标准而且要考虑加工的合理性。这就要求在设计换热器的这就要求工师在选用标准系列设备或设计非定型设备时，结合任务的要求，作管子的外，垢或可以进行化学的场合下用正三角形排列。必须进行机械的场，管子直满足允许的压力降一般选用Ф19mm的管子。对于易结垢的物料，为方便，25mm结垢不是很严重，又允许压力降较高的情况下，采用Φ19mm×2mm的管子是管来壳径较大的换热器采用较长的管子可降低单位传热面积的金属耗量4~6m的管长管心距管心距小设备紧凑但引起管板增厚清洁不便壳压1.25~1.5倍。力降比单壳增加6~8倍。只有壳流量很小，采用最小板间距壳流速仍时，可考虑用两个换热器串联代替双壳温度限冷却水的出口温度不宜高于60℃，以免结垢严重。高温端的温差不应小于20℃5℃温差不应小于20℃。在冷却或者冷凝工艺物流时，冷却剂的温度应高于工5℃的一般低5℃换热器的设计温度应高于最大使15°C。压力降的当工艺物流压力小于9.8×104𝑃𝑎时，允许压力降是9.8×103𝑃𝑎；当工艺物流压力介于9.8×104𝑃𝑎至16.7×104𝑃𝑎之间时，允许压力降介于3.3×103𝑃𝑎3.9×103𝑃𝑎之间；当工艺物流压力大于16.7×104𝑃𝑎时，允许压力降小于9.8×物流安换热器管和壳之间的物流存在一定的限制和要求目的在于强化传除①高温物流，一般走管此有时为了节省保温层和减少壳体厚度，也可以使高温物流走壳除②较高压的物流应走壳在壳可以得到较高的传热系数③较粘的物流应走壳在壳可以得到较高的传热系数④腐蚀性较强的物流应位于管⑤对压力降有特定要求的工艺物流，应位于管因管的传热系数和压以⑥较脏和易结垢的物流应走管便和控制结垢。若必须走壳则以因⑦流量较少的物流应走壳为在壳使物流成为湍流状态，从而增加因⑧给热系数较小的物流，像气体，应走壳于提高给热系数物料流2.1管壳式换热器中常用的流速范流体的种 一般流 易结垢流 气管壳2.2的流速表(管内类管最低流最高流适宜流第三章热器设计举交换器》以及《化工工艺设计手册第二版（下》第四版，使用AspenExchangerDesignandRatingV8.8进行换热设备的设计，以此作为参考从工艺手册上选进行模拟计算，模拟出来的换热器工艺参数操作条壳管MDEA操作条壳管MDEAMDEA质量流量进口温度出口温度进口压力出口压力参 同换热器，封头为椭圆形封头，双管时使用浮头式换热器减少热应力同时便同在考虑流向问题时考虑到冷却物流走管更加合适同时由于富液中溶液吸收了大量硫化氢，具有一定的腐蚀性，因而让MDEA富液走管更和符设计标准。在确定好流体之后，对于类型的选择，EDR3.1针对前封头封头管箱适用于较清洁的介质工况因检查换热管内及换LMLM中，选择浮头式换热器。E必须为偶数。根据介质情况，这里选择E单以艺流体的换热，低温端温差一般高于20℃。采用多管壳水为冷却剂单以，鉴于该换热器的壳工作温度为110℃，管工作温度为50℃温差10℃，温度为160℃，管的设计温度为90℃这里取壳设计压力为0.3MPa,管的设计压力为1.1MPa这里也要考虑压压小于0.1MPa（真空条件压降不大于进口压强的40%，出口绝压大于0.1MPa，20%。表3.2管壳式换热器的合理压 P＝701000Kpa(表 P＝10003000Kpa(表 较高压操 P＝30008000Kpa(表 70和固壁热阻为EDR自动默认值。该换热器的管为冷却水，根据《化工工艺设计手册（第四版）上册，冷却水平均污垢系数为0.00017m2K/W，壳硫同样查0.000073m2K/W。管径与19mm换热时，可选用25mm的管径，这样更方便。3.3用国内换热管的规材标外径mmx厚度19x25x25x19x不锈 25x算，将同直径换热器中的换热管由Φ25mm改为Φ19mm，40%左右，节约20%金属以上；但增加了制造难度，且小管子容易结垢，不易。结垢不是很严重，又允许压力降较高的情况下，采用Φ19mm×2mm的管子是排列形管长一点的管子(12.2m的碳，21.3m的铜合金管)通常只在可以得到。但6m长的换热管则是很普遍的。无相变换热时，管子较长则传热系数也增加，在相同传热面时，采用长管较好，一是可减少管数，二是可减少压力降，三是每平方米传热面的比价低。但是管子过长给制造带来，因此，一般选用4，6m8，9m的管长。在冷凝器管压力降过大，一般选在1～2。由于设计冷凝器，考虑冷凝水的，因此这里走双管比较合理。折流折流板型折流折流板圆置水平放置的折流板适用于无相变的对流传热防止壳流体平行于管束流动，减少壳底部液体沉积。而在带有悬浮物或结垢严重的流体所使用折流板圆缺高15-25％。折流板间1/2TEMA0.8倍。最后根据EDR的设计方案，选择其中较为合理的一组。结合器》规定，选择换热管内径为19mm，壁厚2mm，管心距25mm，排列方式为正三角形，壳工直径（内径）为750mm，壁厚10mm，换热管长度1500mm，折流板间450mm504EDR默认值。计算结165.3m^2，36%，符合设计要求；壳流速为8.04m/s，管流速为5.7m/s，均为湍流态，且满E0101BES700-1.1/0.3-165.3-3/19-（mm（MPa，0.3-（MPa3（m（mm2-双管Ⅰ-Ⅰ级管束详细结

3.2计算结果表（TEMA表3.23.3校核准备资S30408Q345RSW6-2011强度校核3.4入数据项管项管 设计 设 设备直 计算长备输数由SW6-2011计算结果如下表所示（SW6源文件 序文件夹

压力

3.5SW6算结果统计项 计算结果 备设备筒体壁设备筒体壁 详见表5.7,表上封头壁 详见表下封头壁下封头壁 详见表 设备法兰复设备法兰复 合 详见表壳3.6入数据统计壳固定管板换热器计算单位 管设计压力M3设计温度 设计温度mm管箱圆筒内0 壳圆筒校核计3.7段管箱筒体计GB150.3-计算压力设计温度内径 (板材试验温度下屈服点负偏差腐蚀裕量焊接接头系数 =2[]t =e=n-C1-C2=n pT (用户输入的应力水平T0.90ReL pT.(DieT =T2e[]t (Die)=pc(Diet =t3.8端管箱封头计GB150.3-计算压力设计温度内径曲面深度 (板材力力负偏差腐蚀裕量焊接接头系数pT = (或由用户输入a力T0.90ReL apT.(KDi0.5ehT 2eh =aT1 D22i6 2hK i= =2[]t0.5 =heh=nh-C1-C2=min=nh= [p KDi0.5eh=w3.9后端管箱筒体计GB150.3-计算压力设计温度内径 (板材试验温度下屈服点负偏差腐蚀裕量焊接接头系数 =2[]t =e=n-C1-C2=n pT= 的应力水平T0.90ReL pT.(DieT 2e =T2e[]t (Die)=pc(Diet =t3.10后端管箱封头GB150.3-计算压力设计温度内径曲面深度 (板材负偏差腐蚀裕量焊接接头系数pT = (或由用户输入力T0.90ReL pT.(KDi0.5ehT 2eh =T1 D22i6 2hK i= =2[]t0.5 =heh=nh-C1-C2=min=nh= [p KDi0.5eh=w3.11圆筒校GB150.3-计算压力设计温度内径 (板材试验温度下屈服点负偏差腐蚀裕量焊接接头系数 =2[]t =e=n-C1-C2=n pT (或由用户输入的应力水平T0.90ReL pT.(DieT =T2e[]t (Die)=pc(Diet =t3.12管换热管内压计计算压力设计温度外径m (管材m负偏差腐蚀裕量m焊接接头系数 =2[]t =e=n-C1-C2=n 2e[]t =t =t3.13管换热管外压计位计算压力-设计温度外径 (管材试验温度许用应力设计温度许用应力负偏差腐蚀裕量焊接接头系数=e=n-C1-C2=n 外压计算长度 外径Do=A B 当D20时，pD o/e4a当Doe20[p]min{(2.250.0625)B,2o(1 Do/ Do/ Do3.14箱法兰计位N壳体许用应 法兰许应f螺栓许应b个垫片DD内-h片Nmb0b0>6.4mmb=2.53 DGD外+Db0 DGDNNndA=41b操作MpF=0.785D2 iNLD=LA+=-MD=FD=-NLG=0.5(Db-DG=7FT=F-=-NLT=0.5(LA+1+LG=MT=FT=外压:Mp=FD(LD-LG)+FT(LT-LG);内压预紧NLG LG=MaMo=MpMa[]f/[Mt Lnm62.0(GB150-20117-mmLmaxmmh0Di0K=Do/DI=10K7-9ZY7-7-eFIh07-7-eFLh07-由1/od1Uho =d1Uho =f4fe1 =核 结论W D iWp Dli 输入法兰厚度δf=40.0mm时,质 结论HfMo2 1.5[]t=267.0f2.5[]t=300.0(n兰设计的任意式法兰力取n)力R(1.33fe1)M 2f[]t=f力M0YZ 2 Rf[]t=f力[]t=f数J52.14VIMoE2K o13.15换热管壳压力试验外压计直管换热管壳压力试验外压计位计算压力-设计温度外径 (管材试验温度许用应力设计温度许用应力负偏差腐蚀裕量焊接接头系数=e=n-C1-C2=n 外压计算长度 外径Do=A B 当D20时，pD o/e}a当Doe20时[p]min{(2.250.0625)B,2o(1 Do/ Do/ Do/=换热管壳压力试验外压计算合表3.16延长部分兼作法兰固定式管板腐蚀前计位 图简壳设计压 设计温 平均金属温 装配温 设计温度下许用应力c量壳圆筒内径壳圆筒名义厚度壳圆筒有效厚度壳体法兰设计温度下弹性模量 圆筒内直径横截面积A=0.252壳圆筒金属横截面积As=s(Di+s管箱圆筒设计温度下弹性模量管箱圆筒名义厚度(颈部大小端平均值管箱圆筒有效厚度”管箱法兰设计温度下弹性模量管子平均温度设计温度下管子材料许用应力t设计温度下管子材料屈服应力s设计温度下管子材料弹性模量Et平均金属温度下管子材料弹性模量平均金属温度下管子材料热膨胀系数管子外径管子壁厚2管子根数换热管中心距一根管子金属横截面积at(dt换热管长度管子有效长度(两管板内侧间距)管束模数 =Et管子回转半 i0.25d2(d2t管子受压失稳当量长度系 2Et/Cr 比 lcrCr管子稳定许用压应力 i 2t C管子稳定许用压应力( i Rt li[]creL1cr1.5 2Cr设计温度设计温度下许用应力r设计温度下弹性模量管板腐蚀裕量0管板输入厚度管板计算厚度管板分处面积0管板强度削弱系数管板刚度削弱系数管子加强系数K21.32DiEnaE K管板和管子胀接(焊接)2胀接许用拉脱应力焊接许用拉脱应力附件1换热器设计结果一 壳层材1BES700−1.1/0.3–165.3−3/19−2Q345R/2BES500−0.3/0.7–71.5−3/19−2Q345R/3GP9×2–6–140-4.0K1-23.4/DR-1（空冷4BJS750−0.3/1.1−212.6−3/19−2S30408/5BJS850−0.3/0.3–422.4−3/19−1Q345R/6BEM500−0.3/1.1−27.3−1.5/19−1S30408/7BEM600−0.3/1.1−55.2−2/19−1Q345R/8NKN700/850−0.3/0.6–114.0−3/19−1S30408/9BES900−0.3/3.9−100.5−3/19−1S30408/BEM500−0.3/0.3−59.8−2/19−1NKN800/950−0.3/0.6–153.4−3/19−1S30408/序序 位 设备用 型 数量换热管数 壳层材AEN5000.3/0.3–3/19−1S30408/BEM5000.3/0.3–3/19−1BJS7000.3/0.6–3/19−1BES5001.1/0.8–3/19−1BES600−0.3/1.2−111.9–4.5/19−1Q345R/BEM8000.3/0.65168.43/19−2IBES600−1.4/1.4−614.3−4.5/19−1BEM800−1.4/1.7−247.2−3/19−1BEM10001.4/3.9217.23/19−1BEM9001.1/1.4536.76/19−2BEM900−1.4/1.1−438.8−3/19−1Q345R序序 位 设备用 型 数量换热管数 壳层材BEU7001.4/0.3–3/19−1S31608/BEM5000.3/0.3–2/19−1BES6000.1/3.9–3/19−1BEM5000.3/0.3−39.5−3/19−1Serviceof OurItem Rev Job Connected PERFORMANCEOFONEFluid 0000 00Temperature Dew/Bubble Density(Vap/ /// /// Molecularwt,Molecularwt,Specific / Thermal // Latent Pressure Pressuredrop, 0 AoHeat MTD Transferrate, CONSTRUCTIONOFONE Design/vac/test Design Numberpassesper12Corrosion Tks- 3000 CarbonTube Carbon 680 700 CarbonChannelor CarbonChannel CarbonTubesheet- CarbonTubesheet- CarbonFloatinghead Carbon ement Baffle- Carbon Single 41 Spacing: Baffle- Seal Bypass Exp.2Expansion RhoV2-Inlet Bundle Bundle Gaskets- FlatMetalJacket FlatMetalJacketFloating FlatMetalJacketCode ASMECodeSecVIIIDiv TEMA R-refinery Filledwith 附件2换热器设计TEMAE0101HeatExchangerSpecification123456 8 42 E0102HeatExchangerSpecificationServiceof OurItem Rev Job Connected PERFORMANCEOFONEFluid 00 00Temperature Dew/Bubble -Density(Vap/ / / Molecularwt,Molecularwt,Specific / Thermal / Latent Pressure Pressuredrop, 0 AoHeat MTD Transferrate, CONSTRUCTIONOFONE Design/vac/test Design Numberpassesper12Corrosion 1 254.51 1 254.51 2.11 3000 CarbonTube Carbon 480 500 CarbonChannelor CarbonChannel CarbonTubesheet- CarbonTubesheet- CarbonFloatinghead Carbon ement Baffle- Carbon Single 23 Spacing: Baffle- Seal Bypass Exp.2Expansion RhoV2-Inlet Bundle Bundle Gaskets- FlatMetalJacketF FlatMetalJacketFloating FlatMetalJacketFCode ASMECodeSecVIIIDiv TEMA R-refinery Filledwith 23456 8 42 E0103Air-CooledHeatExchangerSpecificationServiceof OurItem Rev JobSize&Type Surf/Unit-Finned Heat Bare,Bare Numberof MTD, 4PERFORMANCEDATA-TUBEFluid / SpecificHeat, SpecificHeat,/ Therm.Cond, Therm.Cond,//FreezeC Bubble/DewC/Molecularwt, LatentMolecularwt,Inletpressure PresDrop, 0 Static Temperature Face 4.24 Bundle Design DESIGN-MATERIALS-Design Design TUBE Carbon Carbon Min Plug Gasket Corr. BundleInlet 1G-Outlet 1AluminumStruct.Special 433 C ChemMECHANICALSpeedReducer, 31.497kWControlActiononAirDegreeControlofOutletProcessPlot m2Drawing Wt. 2345678918 E0104E0104HeatExchangerSpecificationServiceof OurItem Rev Job Connected PERFORMANCEOFONEFluid Process 0 0 00Temperature Dew/Bubble Density(Vap/ / / Molecularwt,Molecularwt,Specific / Thermal / Latent Pressure Pressuredrop, 0 AoHeat MTD Transferrate, CONSTRUCTIONOFONE Design/vac/test Design Numberpassesper12Corrosion 00 1 254.51 2 590.55 1.65 3000 SSTube SS 735 750 SSChannelor SSChannel SSTubesheet- SSTubesheet- SSFloatinghead SSImement Baffle- SS Single 19 Spacing: Baffle- Seal Bypass Exp.2Expansion RhoV2-Inlet Bundle Bundle Gaskets-S FlatMetalJacket FlatMetalJacketFloating FlatMetalJacketCode ASMECodeSecVIIIDiv TEMA R-refineryWeight/S Filledwith 123456 8 42 E0105E0105HeatExchangerSpecificationServiceof OurItem Rev Job Connected PERFORMANCEOFONEFluid 00 00Temperature Dew/Bubble -Density(Vap/ / / Molecularwt,Molecularwt,Specific / Thermal / Latent Pressure 1 Pressuredrop, 0 AoHeat MTD Transferrate, CONSTRUCTIONOFONE Design/vac/test Design Numberpassesper12Corrosion 00 2 438.15 1 438.15 1.65 3000 SSTube SS 835 850 SSChannelor SSChannel SSTubesheet- SSTubesheet- SSFloatinghead SSImement Baffle- SS Single 25 Spacing: Baffle- Seal Bypass Exp.2Expansion RhoV2-Inlet Bundle Bundle Gaskets-S FlatMetalJacket FlatMetalJacketFloating FlatMetalJacketCode ASMECodeSecVIIIDiv TEMA R-refineryWeight/S Filledwith 123456 8 42 E0201E0201HeatExchangerSpecificationServiceof OurItem Rev Job Connected PERFORMANCEOFONEFluid 0 000 00Temperature Dew/Bubble Density(Vap/ / Molecularwt,Molecularwt,Specific / Thermal Latent Pressure Pressuredrop, 0 AoHeat MTD Transferrate, CONSTRUCTIONOFONE Design/vac/test Design Numberpassesper11Corrosion 00 1 202.72 1 202.72 1.65 2000 SSTube SS 580 600 Channelor SSChannel Tubesheet- SSTubesheet- Floatinghead Imement Baffle- SS Single 43 Spacing: Baffle- Seal Bypass Exp.2Expansion RhoV2-Inlet Bundle Bundle Gaskets-S FlatMetalJacketFloating Code ASMECodeSecVIIIDiv TEMA R-refineryWeight/S Filledwith 123456 8 42 E0203E0203HeatExchangerSpecificationServiceof OurItem Rev Job Connected PERFORMANCEOFONEFluid 0 000 00Temperature Dew/Bubble Density(Vap/ / / Molecularwt,Molecularwt,Specific / Thermal / Latent Pressure Pressuredrop, 0 AoHeat MTD Transferrate, CONSTRUCTIONOFONE Design/vac/test Design Numberpassesper11Corrosion 1 254.51 1 254.51 2.11 1500 CarbonTube Carbon 480 500 Channelor CarbonChannel Tubesheet- CarbonTubesheet- Floatinghead Imement Baffle- Carbon Single 37 Spacing: Baffle- Seal Bypass Exp.2Expansion RhoV2-Inlet Bundle Bundle Gaskets-S FlatMetalJacketFFloating Code ASMECodeSecVIIIDiv TEMA R-refineryWeight/S Filledwith 123456 8 42 E0204E0204HeatExchangerSpecificationServiceof OurItem Rev Job / Connected PERFORMANCEOFONEFluid CW- 0 0 00Temperature Dew/Bubble Density(Vap/ / / Molecularwt,Molecularwt,Specific / Thermal / Latent Pressure 5 Pressuredrop, 0 AoHeat MTD Transferrate, CONSTRUCTIONOFONE Design/vac/test Design Numberpassesper11Corrosion 0 1 336.55 1 336.55 Tks- 1.65 3000 SSTube Carbon 680 700 Channelor CarbonChannel CarbonTubesheet- CarbonTubesheet- Floatinghead Imement Baffle- Carbon Spacing: Baffle- Seal Bypass Exp.2Expansion RhoV2-Inlet Bundle Bundle Gaskets-S FlatMetalJacketFloating Code ASMECodeSecVIIIDiv TEMA R-refineryWeight/S Filledwith 123456 8 42 E0205E0205HeatExchangerSpecificationServiceof OurItem Rev Job Connected PERFORMANCEOFONEFluid 2- 0 000 00Temperature Dew/Bubble Density(Vap/ / / Molecularwt,Molecularwt,Specific / Thermal / Latent Pressure Pressuredrop, 0 AoHeat MTD Transferrate, CONSTRUCTIONOFONE Design/vac/test Design Numberpassesper14Corrosion 1 336.55 1 336.55 2.11 3000 CarbonTube Carbon 880 900 CarbonChannelor CarbonChannel CarbonTubesheet- CarbonTubesheet- CarbonFloatinghead CarbonImement Baffle- Carbon Single 20 Spacing: Baffle- Seal Bypass Exp.2Expansion RhoV2-Inlet Bundle Bundle Gaskets-S FlatMetalJacket FlatMetalJacketFloating FlatMetalJacketCode ASMECodeSecVIIIDiv TEMA R-refineryWeight/S Filledwith 123456 8 42 E0206E0206HeatExchangerSpecificationServiceof OurItem Rev Job Connected PERFORMANCEOFONEFluid 0000 00Temperature Dew/Bubble -Density(Vap/ / / Molecularwt,Molecularwt,Specific / Thermal / Latent Pressure Pressuredrop, 0 AoHeat MTD Transferrate, CONSTRUCTIONOFONE Design/vac/test Design Numberpassesper11Corrosion 00 1 202.72 1 202.72 1.65 2000 SSTube SS 480 500 Channelor SSChannel Tubesheet- SSTubesheet- Floatinghead Imement Baffle- SS Single 41 Spacing: Baffle- Seal Bypass Exp.2Expansion RhoV2-Inlet Bundle Bundle Gaskets-S FlatMetalJacketFloating Code ASMECodeSecVIIIDiv TEMA R-refineryWeight/S Filledwith 123456 8 42 E0207E0207HeatExchangerSpecificationServiceof OurItem Rev Job / Connected PERFORMANCEOFONEFluid CW- 0 0 00Temperature Dew/Bubble Density(Vap/ / / Molecularwt,Molecularwt,Specific / Thermal / Latent Pressure 5 Pressuredrop, 0 AoHeat MTD Transferrate, CONSTRUCTIONOFONE Design/vac/test Design Numberpassesper11Corrosion 0 1 304.8 1 304.8 1.65 3000 SSTube Carbon 780 800 Channelor CarbonChannel CarbonTubesheet- CarbonTubesheet- Floatinghead Imement Baffle- Carbon Spacing: Baffle- Seal Bypass Exp.2Expansion RhoV2-Inlet Bundle Bundle Gaskets-S FlatMetalJacketFloating Code ASMECodeSecVIIIDiv TEMA R-refineryWeight/S Filledwith 123456 8 42 E0208E0208HeatExchangerSpecificationServiceof OurItem Rev Job Connected PERFORMANCEOFONEFluid 00 0 00Temperature Dew/Bubble -Density(Vap/ / / Molecularwt,Molecularwt,Specific / Thermal / Latent Pressure 1 Pressuredrop, 0 AoHeat MTD Transferrate, CONSTRUCTIONOFONE Design/vac/test Design Numberpassesper12Corrosion 0 1 90.12 1 90.12 1.65 3000 SSTube Carbon 475 500 Channelor CarbonChannel CarbonTubesheet- CarbonTubesheet- Floatinghead Imement Baffle- Carbon Single 42 Spacing: Baffle- Seal Bypass Exp.2Expansion RhoV2-Inlet Bundle Bundle Gaskets-S FlatMetalJacketFloating Code ASMECodeSecVIIIDiv TEMA R-refineryWeight/S Filledwith 123456 8 42 E0209E0209HeatExchangerSpecificationServiceof OurItem Rev Job Connected PERFORMANCEOFONEFluid 0000 00Temperature Dew/Bubble Density(Vap/ / / Molecularwt,Molecularwt,Specific / Thermal / Latent Pressure Pressuredrop, 0 AoHeat MTD Transferrate, CONSTRUCTIONOFONE Design/vac/test Design Numberpassesper12Corrosion 00 1 154.05 1 154.05 1.65 3000 SSTube SS 480 500 Channelor SSChannel Tubesheet- SSTubesheet- Floatinghead Imement Baffle- SS Single 42 Spacing: Baffle- Seal Bypass Exp.2Expansion RhoV2-Inlet Bundle Bundle Gaskets-S FlatMetalJacketFloating Code ASMECodeSecVIIIDiv TEMA R-refineryWeight/S Filledwith 123456 8 42 E0210E0210HeatExchangerSpecificationServiceof OurItem Rev Job Connected PERFORMANCEOFONEFluid CW- 0 000 00Temperature Dew/Bubble Density(Vap/ / / Molecularwt,Molecularwt,Specific / Thermal / Latent Pressure 5 Pressuredrop, 0 AoHeat MTD Transferrate, CONSTRUCTIONOFONE Design/vac/test Design Numberpassesper12Corrosion 0 2 336.55 1 336.55 1.65 3000 SSTube Carbon 680 700 CarbonChannelor CarbonChannel CarbonTubesheet- CarbonTubesheet- CarbonFloatinghead CarbonImement Baffle- Carbon Single 20 Spacing: Baffle- Seal Bypass Exp.2Expansion RhoV2-Inlet Bundle Bundle Gaskets-S FlatMetalJacket FlatMetalJacketFloating FlatMetalJacketCode ASMECodeSecVIIIDiv TEMA R-refineryWeight/S Filledwith 123456 8 42 E0211E0211HeatExchangerSpecificationServiceof OurItem Rev Job Connected PERFORMANCEOFONEFluid 0000 00Temperature Dew/Bubble Density(Vap/ / / Molecularwt,Molecularwt,Specific Thermal / Latent Pressure Pressuredrop, 0 AoHeat MTD Transferrate, CONSTRUCTIONOFONE Design/vac/test Design Numberpassesper12Corrosion 0 1 202.72 1 202.72 1.65 3000 SSTube Carbon 480 500 CarbonChannelor CarbonChannel CarbonTubesheet- CarbonTubesheet- CarbonFloatinghead CarbonImement Baffle- Carbon Single 21 Spacing: Baffle- Seal Bypass Exp.2Expansion RhoV2-Inlet Bundle Bundle Gaskets-S FlatMetalJacket FlatMetalJacketFloating FlatMetalJacketCode ASMECodeSecVIIIDiv TEMA R-refineryWeight/S Filledwith 123456 8 42 E0212E0212HeatExchangerSpecificationServiceof OurItem Rev Job Connected PERFORMANCEOFONEFluid 0000 00Temperature Dew/Bubble Density(Vap/ / / Molecularwt,Molecularwt,Specific / Thermal / Latent Pressure 1 Pressuredrop, 0 AoHeat MTD Transferrate, CONSTRUCTIONOFONE Design/vac/test Design Numberpassesper12Corrosion 1 154.05 1 154.05 2.11 4500 CarbonTube Carbon 580 600 CarbonChannelor CarbonChannel CarbonTubesheet- CarbonTubesheet- CarbonFloatinghead CarbonImement Baffle- Carbon Single 26 Spacing: Baffle- Seal Bypass Exp.2Expansion RhoV2-Inlet Bundle Bundle Gaskets-S FlatMetalJacket FlatMetalJacketFloating FlatMetalJacketCode ASMECodeSecVIIIDiv TEMA R-refineryWeight/S Filledwith 123456 8 42 E0301E0301HeatExchangerSpecificationServiceof OurItem Rev Job Connected PERFORMANCEOFONEFluid LP-3- 0 0 00Temperature Dew/Bubble -Density(Vap/ / / Molecularwt,Molecularwt,Specific / Thermal Latent Pressure 51 Pressuredrop, 0 AoHeat MTD Transferrate, CONSTRUCTIONOFONE Design/vac/test Design Numberpassesper11Corrosion 1 539.75 1 539.75 2.11 3000 CarbonTube Carbon 785 800 Channelor CarbonChannel Tubesheet- CarbonTubesheet- Floatinghead Imement Baffle- Carbon Single 39 Spacing: Baffle- Seal Bypass Exp.2Expansion RhoV2-Inlet Bundle Bundle Gaskets-S FlatMetalJacketFloating Code ASMECodeSecVIIIDiv TEMA R-refineryWeight/S Filledwith 123456 8 42 E0302E0302HeatExchangerSpecificationServiceof OurItem Rev Job Connected PERFORMANCEOFONEFluid S35-S18- 000 00Temperature Dew/Bubble Density(Vap/ // / Molecularwt,Molecularwt,Specific / Thermal // Latent Pressure Pressuredrop, 0 AoHeat MTD Transferrate, CONSTRUCTIONOFONE Design/vac/test 14 Design Numberpassesper11Corrosion 1 304.8 1 304.8 2.11 4.5 CarbonTube Carbon 0.58 0.6 CarbonChannelor CarbonChannel CarbonTubesheet- CarbonTubesheet- CarbonFloatinghead CarbonImement Baffle- Carbon Single 39 Spacing: Baffle- Seal Bypass Exp.2Expansion RhoV2-Inlet Bundle Bundle Gaskets-S FlatMetalJacketF FlatMetalJacketFloating FlatMetalJacketFCode ASMECodeSecVIIIDiv TEMA R-refineryWeight/S Filledwith 123456 8 42 E0303E0303HeatExchangerSpecificationServiceof OurItem Rev Job Connected PERFORMANCEOFONEFluid S26-S18- 000 0 00Temperature Dew/Bubble Density(Vap/ / / Molecularwt,Molecularwt,Specific / Thermal / Latent Pressure Pressuredrop, 0 AoHeat MTD Transferrate, CONSTRUCTIONOFONE Design/vac/test 14 Design Numberpassesper11Corrosion 1 488.95 1 488.95 2.11 3000 CarbonTube Carbon 775 800 Channelor CarbonChannel Tubesheet- CarbonTubesheet- Floatinghead Imement Baffle- Carbon Single 39 Spacing: Baffle- Seal Bypass Exp.2Expansion RhoV2-Inlet Bundle Bundle Gaskets-S FlatMetalJacketFloating Code ASMECodeSecVIIIDiv TEMA R-refineryWeight/S Filledwith 123456 8 42 E0304E0304HeatExchangerSpecificationServiceof OurItem Rev Job Connected PERFORMANCEOFONEFluid S18- 000 0 00Temperature Dew/Bubble Density(Vap/ / / Molecularwt,Molecularwt,Specific Thermal / Latent Pressure Pressuredrop, 0 AoHeat MTD Transferrate, CONSTRUCTIONOFONE Design/vac/test 14 Design Numberpassesper11Corrosion 1 641.35 1 641.35 2.11 CarbonTube Carbon 968 1000 Channelor CarbonChannel Tubesheet- CarbonTubesheet- Floatinghead Imement Baffle- Carbon Single 39 Spacing: Baffle- Seal Bypass Exp.2Expansion RhoV2-Inlet Bundle Bundle Gaskets-S FlatMetalJacketFloating Code ASMECodeSecVIIIDiv TEMA R-refineryWeight/S Filledwith 123456 8 42 E0305E0305HeatExchangerSpecificationServiceof OurItem Rev Job HorConnected PERFORMANCEOFONEFluid 00 0 00Temperature Dew/Bubble Density(Vap/ / / Molecularwt,Molecularwt,Specific / Thermal / Latent Pressure Pressuredrop, 0 AoHeat MTD Transferrate, CONSTRUCTIONOFONE Design/vac/test 11 Design Numberpassesper11Corrosion 1 90.12 1 254.51 1 202.72 2.11 6000 CarbonTube Carbon 880 900 Channelor CarbonChannel Tubesheet- CarbonTubesheet- Floatinghead Imement Baffle- Carbon Single 41 Spacing: Baffle- Seal Bypass Exp.2Expansion RhoV2-Inlet Bundle Bundle Gaskets-S FlatMetalJacketFloating Code ASMECodeSecVIIIDiv TEMA R-refineryWeight/S Filledwith 123456 8 42 E0306E0306HeatExchangerSpecificationServiceof OurItem Rev Job Connected PERFORMANCEOFONEFluid 00 0 00Temperature Dew/Bubble Density(Vap/ / / Molecularwt,Molecularwt,Specific / Thermal / Latent Pressure Pressuredrop, 0 AoHeat MTD Transferrate, CONSTRUCTIONOFONE Design/vac/test Design Numberpassesper14Corrosion 1 202.72 1 77.93 2.11 CarbonTube Carbon 875 900 Channelor CarbonChannel Tubesheet- CarbonTubesheet- Floatinghead Imement Baffle- Carbon Single 41 Spacing: Baffle- Seal Bypass Exp.2Expansion RhoV2-Inlet Bundle Bundle Gaskets-S FlatMetalJacketFloating Code ASMECodeSecVIIIDiv TEMA R-refineryWeight/S Filledwith 123456 8 42 E0307E0307HeatExchangerSpecificationServiceof OurItem Rev Job Connected PERFORMANCEOFONEFluid S35- 0000 00Temperature Dew/Bubble Density(Vap/ / / Molecularwt,Molecularwt,Specific / Thermal / Latent Pressure Pressuredrop, 0 AoHeat MTD Transferrate, CONSTRUCTIONOFONE Design/vac/test Design Numberpa