[{"data":1,"prerenderedAt":320},["ShallowReactive",2],{"\u002Fblog\u002Fgtnh\u002Fbenzene":3,"article-navigation:\u002Fblog\u002Fgtnh\u002Fbenzene":318},{"id":4,"title":5,"album":6,"albumIndex":7,"body":8,"category":302,"cover":303,"coverAlt":303,"coverCaption":303,"date":304,"description":305,"draft":7,"extension":306,"home":7,"homeFacts":307,"homeImage":308,"homeNote":303,"meta":309,"navigation":310,"path":311,"seo":312,"stem":313,"tags":314,"updated":303,"__hash__":317},"blog\u002Fblog\u002Fgtnh\u002Fbenzene.md","热解苯与木材干馏","gtnh",false,{"type":9,"value":10,"toc":288},"minimark",[11,15,20,25,92,122,128,135,148,157,166,170,180,183,203,206,210,217,220,224,228,248,255,258],[12,13,14],"p",{},"油源不方便、有树场时，MV 可以用热解苯发电：先无氮运行，苯不够再加氮。HV 升级蒸馏塔，保留其他化工馏分。",[16,17,19],"h2",{"id":18},"mv-中期热解与供氮","MV 中期：热解与供氮",[21,22,24],"h3",{"id":23},"主电源方案一热解苯起步","主电源方案一：热解苯起步",[26,27,28,44],"table",{},[29,30,31],"thead",{},[32,33,34,38,41],"tr",{},[35,36,37],"th",{},"机器\u002F配置",[35,39,40],{},"输入 → 输出",[35,42,43],{},"原始参数",[45,46,47,59,70,81],"tbody",{},[32,48,49,53,56],{},[50,51,52],"td",{},"热解炉，电路 9",[50,54,55],{},"16 原木 → 20 木炭 + 1500 L 木焦油",[50,57,58],{},"64 EU\u002Ft，32 秒",[32,60,61,64,67],{},[50,62,63],{},"热解炉，电路 10",[50,65,66],{},"16 原木 + 1000 L 氮 → 相同产物",[50,68,69],{},"96 EU\u002Ft，16 秒",[32,71,72,75,78],{},[50,73,74],{},"流体提取机",[50,76,77],{},"1 木炭 → 100 L 木焦油，10% 概率出灰",[50,79,80],{},"15 EU\u002Ft，30 tick",[32,82,83,86,89],{},[50,84,85],{},"MV 蒸馏室，电路 3",[50,87,88],{},"100 L 木焦油 → 40 L 苯",[50,90,91],{},"64 EU\u002Ft，8 tick",[12,93,94,98,99,103,104,111,112,111,117],{},[95,96,97],"strong",{},"先用电路 9 无氮运行；有稳定氮再切 10。"," 实际供氮速度按 ",[100,101,102],"code",{},"1000 L÷每批秒数"," 配。 ",[105,106,110],"a",{"href":107,"rel":108},"https:\u002F\u002Fgithub.com\u002FGTNewHorizons\u002FGT5-Unofficial\u002Fblob\u002F5.09.54.205\u002Fsrc\u002Fmain\u002Fjava\u002Fgregtech\u002Floaders\u002Fpostload\u002Frecipes\u002FPyrolyseRecipes.java",[109],"nofollow","热解"," · ",[105,113,116],{"href":114,"rel":115},"https:\u002F\u002Fgithub.com\u002FGTNewHorizons\u002FGT5-Unofficial\u002Fblob\u002F5.09.54.205\u002Fsrc\u002Fmain\u002Fjava\u002Fgregtech\u002Floaders\u002Fpostload\u002Frecipes\u002FFluidExtractorRecipes.java",[109],"木炭流体提取",[105,118,121],{"href":119,"rel":120},"https:\u002F\u002Fgithub.com\u002FGTNewHorizons\u002FGT5-Unofficial\u002Fblob\u002F5.09.54.205\u002Fsrc\u002Fmain\u002Fjava\u002Fgregtech\u002Floaders\u002Fpostload\u002Frecipes\u002FDistilleryRecipes.java",[109],"木焦油蒸馏",[12,123,124,127],{},[95,125,126],{},"每 16 原木的理论收支："," 热解先得 1500 L 木焦油；20 木炭全提取再得 2000 L；合计 3500 L 木焦油，按 40% 变为 1400 L 苯。若锅炉还要吃木炭，必须从这 20 木炭中分走一部分，苯收益相应减少。",[12,129,130,131,134],{},"起步建 ",[95,132,133],{},"热解炉 1＋流体提取机 1＋MV 蒸馏室 1","。木炭积压先加提取机：单台提取 20 木炭需 30 秒，有氮热解原始只需 16 秒出一批。",[12,136,137,111,142,147],{},[105,138,141],{"href":139,"rel":140},"https:\u002F\u002Fgtnh.huijiwiki.com\u002Fwiki\u002F%E7%83%AD%E8%A7%A3%E7%82%89",[109],"热解炉结构",[105,143,146],{"href":144,"rel":145},"https:\u002F\u002Fgtnh.huijiwiki.com\u002Fwiki\u002F%E5%A4%A7%E4%BC%97%E7%94%9F%E7%89%A9%E5%AD%A6\u002F%E6%9C%A8%E6%9D%90%E5%B9%B2%E9%A6%8F",[109],"木化分流","。",[12,149,150],{},[151,152],"img",{"alt":153,"height":154,"src":155,"width":156},"GTNH 中文 Wiki 热解炉结构示意：机械方块、线圈、框架与管道位置",665,"\u002Fuploads\u002Fgtnh-2-9\u002Fpyrolyse-oven.png",600,[12,158,159,160,165],{},"图：热解炉结构；仓室和线圈按 2.9 控制器投影安装。来源：",[105,161,164],{"href":162,"rel":163},"https:\u002F\u002Fgtnh.huijiwiki.com\u002Fwiki\u002F%E6%96%87%E4%BB%B6:%E7%83%AD%E8%A7%A3%E7%82%89%E7%BB%93%E6%9E%84%E5%AF%BC%E5%87%BA.png",[109],"GTNH 中文 Wiki 原图文件页","；上传者 Lekior。",[21,167,169],{"id":168},"热解提速氮源够了再换电路-10","热解提速：氮源够了再换电路 10",[12,171,172,175,176,147],{},[95,173,174],{},"氮罐见底就暂换电路 9。"," 有氮基础需求 62.5 L\u002Fs，基础空气离心段为 48.75 L\u002Fs；扩气源后再切回电路 10。",[105,177,179],{"href":178},"\u002Fblog\u002Fgtnh\u002Fbasic-chemistry","制氮接法",[12,181,182],{},"按以下顺序接氮：",[184,185,186,190,193,200],"ol",{},[187,188,189],"li",{},"先用电路 9 做出苯，接燃气轮机。",[187,191,192],{},"空气分离接好氧单元出口，氮存罐。",[187,194,195,196,199],{},"换电路 10，记录每批秒数，按 ",[100,197,198],{},"1000÷秒数"," 配供氮。",[187,201,202],{},"氮罐持续下降就加气源，或换回电路 9；线圈／能源仓升级后重算一次。",[12,204,205],{},"氮断供先查空单元回流与氧单元出口，再加离心机。",[21,207,209],{"id":208},"给锅炉留木炭后还能产多少苯","给锅炉留木炭后，还能产多少苯",[211,212,214],"collapse",{"title":213},"查看木炭分流的产量计算",[12,215,216],{},"每批热解的 20 木炭若留 8 个给锅炉，剩余 12 个提取成 1200 L 木焦油，加上热解直接产出的 1500 L，共 2700 L；按 40% 蒸馏得到 1080 L 苯。相比全部木炭提取的 1400 L，少 320 L。",[12,218,219],{},"把木炭输出先分为锅炉库存和提取库存，锅炉达到保有量后，余下木炭送提取机。苯罐仍下降时，分别查看原木、木炭、木焦油三个库存：原木缺是树场问题，木炭堆积扩提取，木焦油堆积扩蒸馏。",[16,221,223],{"id":222},"hv-中期保留木化资源","HV 中期：保留木化资源",[21,225,227],{"id":226},"热解苯升级蒸馏塔保留多种馏分","热解苯升级：蒸馏塔保留多种馏分",[12,229,230,231,234,235,238,239,242,243,147],{},"升级到 HV 蒸馏塔后，一张电路 1 配方能把 ",[100,232,233],{},"1000 L 木焦油","同时分成 ",[100,236,237],{},"250 杂酚油 + 100 苯酚 + 400 苯 + 100 甲苯 + 150 二甲苯","，基础 ",[100,240,241],{},"256 EU\u002Ft、2 秒","。苯的比例仍为 40%；升级的好处是同时收集其他馏分，其中苯酚可用于环氧。各层出口接独立罐。",[105,244,247],{"href":245,"rel":246},"https:\u002F\u002Fgithub.com\u002FGTNewHorizons\u002FGT5-Unofficial\u002Fblob\u002F5.09.54.205\u002Fsrc\u002Fmain\u002Fjava\u002Fgregtech\u002Floaders\u002Fpostload\u002Frecipes\u002FDistilleryRecipes.java#L582-L591",[109],"木焦油蒸馏塔配方",[12,249,250,147],{},[105,251,254],{"href":252,"rel":253},"https:\u002F\u002Fgtnh.huijiwiki.com\u002Fwiki\u002F%E8%92%B8%E9%A6%8F%E5%A1%94",[109],"蒸馏塔高度与各层出口",[16,256,257],{"id":257},"接下来读什么",[259,260,261,267,272,278],"ul",{},[187,262,263],{},[105,264,266],{"href":265},"\u002Fblog\u002Fgtnh\u002Fmv#%E6%9C%AC%E9%98%B6%E6%AE%B5%E5%8F%91%E7%94%B5%E6%96%B9%E6%A1%88","MV：石化与热解替代路线",[187,268,269],{},[105,270,271],{"href":178},"基础气体与化工",[187,273,274],{},[105,275,277],{"href":276},"\u002Fblog\u002Fgtnh\u002Fpower-and-logistics","电力与持续产线",[187,279,280,111,284],{},[105,281,283],{"href":282},"\u002Fblog\u002Fgtnh\u002Fmv","主线：MV 阶段",[105,285,287],{"href":286},"\u002Fblog\u002Fgtnh\u002Fhv","主线：HV 阶段",{"title":289,"searchDepth":290,"depth":290,"links":291},"",2,[292,298,301],{"id":18,"depth":290,"text":19,"children":293},[294,296,297],{"id":23,"depth":295,"text":24},3,{"id":168,"depth":295,"text":169},{"id":208,"depth":295,"text":209},{"id":222,"depth":290,"text":223,"children":299},[300],{"id":226,"depth":295,"text":227},{"id":257,"depth":290,"text":257},"games",null,"2026-10-29","从 MV 无氮热解起步，再计算氮气供需、木炭提取与蒸馏瓶颈，最后升级 HV 多馏分蒸馏塔。","md",[],{"src":155,"alt":153,"caption":153,"width":156,"height":154},{},true,"\u002Fblog\u002Fgtnh\u002Fbenzene",{"title":5,"description":305},"blog\u002Fgtnh\u002Fbenzene",[6,315,316],"guide","minecraft","VPbNM3tBKZ-2PChGFQ5c3BvKTZGxD-2yHUXh6i6Glkw",{"newer":303,"older":303,"related":319},[],1793292207881]