[{"data":1,"prerenderedAt":422},["ShallowReactive",2],{"\u002Fblog\u002Fgtnh\u002Fadvanced-chemistry":3,"article-navigation:\u002Fblog\u002Fgtnh\u002Fadvanced-chemistry":420},{"id":4,"title":5,"album":6,"albumIndex":7,"body":8,"category":405,"cover":406,"coverAlt":406,"coverCaption":406,"date":407,"description":408,"draft":7,"extension":409,"home":7,"homeFacts":410,"homeImage":406,"homeNote":406,"meta":411,"navigation":412,"path":413,"seo":414,"stem":415,"tags":416,"updated":406,"__hash__":419},"blog\u002Fblog\u002Fgtnh\u002Fadvanced-chemistry.md","首批 PTFE、硅橡胶与环氧","gtnh",false,{"type":9,"value":10,"toc":387},"minimark",[11,15,20,25,28,36,118,132,135,139,145,164,172,176,180,189,193,200,204,208,213,261,264,271,280,284,291,345,351,354],[12,13,14],"p",{},"HV 早期先用小化反做 PTFE，建成 LCR 后生产硅橡胶并扩产 PTFE；EV 再做环氧。",[16,17,19],"h2",{"id":18},"hv-早期首批材料与第一台-lcr","HV 早期：首批材料与第一台 LCR",[21,22,24],"h3",{"id":23},"首批-ptfe先用-mv-小化反做","首批 PTFE：先用 MV 小化反做",[12,26,27],{},"首批 PTFE 用 MV 单方块化反分四步制作；LCR 建好后，合并其中的前驱体反应。",[12,29,30,31,35],{},"备 ",[32,33,34],"strong",{},"MV 化反 1 台、装罐机、空单元和储罐","，按下表顺序共用化反。",[37,38,39,58],"table",{},[40,41,42],"thead",{},[43,44,45,49,52,55],"tr",{},[46,47,48],"th",{},"步骤",[46,50,51],{},"配置与输入",[46,53,54],{},"输出",[46,56,57],{},"原始参数",[59,60,61,76,90,104],"tbody",{},[43,62,63,67,70,73],{},[64,65,66],"td",{},"甲烷氯化",[64,68,69],{},"电路 13；1 甲烷单元 + 6000 L 氯",[64,71,72],{},"1 氯仿单元 + 3000 L 盐酸",[64,74,75],{},"30 EU\u002Ft，4 秒",[43,77,78,81,84,87],{},[64,79,80],{},"制 HF",[64,82,83],{},"电路 1；1 氟单元 + 1000 L 氢",[64,85,86],{},"1000 L 氢氟酸 + 空单元",[64,88,89],{},"7 EU\u002Ft，3 秒",[43,91,92,95,98,101],{},[64,93,94],{},"制 TFE",[64,96,97],{},"4 氢氟酸单元 + 2 空单元 + 2000 L 氯仿；无需配置电路",[64,99,100],{},"1000 L 四氟乙烯 + 6 盐酸单元",[64,102,103],{},"120 EU\u002Ft，24 秒",[43,105,106,109,112,115],{},[64,107,108],{},"聚合",[64,110,111],{},"电路 1；1 氧单元 + 144 L 四氟乙烯",[64,113,114],{},"216 L 熔融 PTFE + 空单元",[64,116,117],{},"30 EU\u002Ft，8 秒",[12,119,120,121,124,125],{},"这批先备 ",[32,122,123],{},"2 甲烷单元、12000 L 氯、4 氟单元、4000 L 氢和 6 氧单元","，另备空单元周转。甲烷氯化做两次，把氯仿单元卸成 2000 L 流体；制 HF 做四次，灌成 4 个单元。两者制成 1000 L TFE 后，聚合六次消耗 864 L，得到 1296 L PTFE；余下 136 L TFE 留罐。按所需部件选择固化模具，模具不会消耗。",[126,127,131],"a",{"href":128,"rel":129},"https:\u002F\u002Fgithub.com\u002FGTNewHorizons\u002FGT5-Unofficial\u002Fblob\u002F5.09.54.205\u002Fsrc\u002Fmain\u002Fjava\u002Fgregtech\u002Floaders\u002Fpostload\u002Frecipes\u002FChemicalRecipes.java",[130],"nofollow","RC-2 PTFE 注册配方",[12,133,134],{},"两次氯化产生 6000 L 盐酸，制 TFE 又产出 6 个盐酸单元；分别接出口并收集。共用化反换配方前，先抽出上一反应的流体。",[21,136,138],{"id":137},"首台-lcr-与硅橡胶","首台 LCR 与硅橡胶",[12,140,141,144],{},[32,142,143],{},"首台 LCR 轮流做常用化学品。"," 各流体用独立输入仓，副产酸各接储罐；高频配方再拆专机。",[12,146,147,150,151,155,156,159,160],{},[32,148,149],{},"硅橡胶量产例："," LCR 电路 24，",[152,153,154],"code",{},"1 硅粉 + 2000 L 甲烷 + 4000 L 氯 + 1000 L 水 → 3 聚二甲基硅氧烷末 + 2000 L 盐酸 + 2000 L 稀盐酸","，96 EU\u002Ft、24 秒；再将 ",[152,157,158],{},"9 聚二甲基硅氧烷末 + 1 硫粉 → 1296 L 熔融硅橡胶","，30 EU\u002Ft、30 秒。前一步跑三次才够后一批。按所需线缆与部件的可接受橡胶类型分配产量。",[126,161,163],{"href":128,"rel":162},[130],"RC-2 合并化工配方",[12,165,166,171],{},[126,167,170],{"href":168,"rel":169},"https:\u002F\u002Fgtnh.huijiwiki.com\u002Fwiki\u002F%E5%A4%A7%E5%9E%8B%E5%8C%96%E5%AD%A6%E5%8F%8D%E5%BA%94%E9%87%9C",[130],"LCR 结构与仓室位置","。",[16,173,175],{"id":174},"hv-中期至-ev-早期改善-ptfe-生产","HV 中期至 EV 早期：改善 PTFE 生产",[21,177,179],{"id":178},"ptfe-合并前驱体配方","PTFE 合并前驱体配方",[12,181,182,150,185,188],{},[32,183,184],{},"制 TFE：",[152,186,187],{},"2000 L 甲烷＋12000 L 氯＋4000 L 氢氟酸→1000 L TFE＋12000 L 盐酸","，120 EU\u002Ft、27 秒。TFE 输出接聚合机，盐酸回酸库。",[21,190,192],{"id":191},"已有-ticl-后的-ptfe-增产","已有 TiCl₄ 后的 PTFE 增产",[12,194,195,196,199],{},"钛线有余量后，PTFE 改用 LCR 电路 2：",[152,197,198],{},"2160 L TFE＋7500 L 氧＋100 L TiCl₄→4320 L PTFE","，30 EU\u002Ft、40 秒。每批补 100 L TiCl₄。",[16,201,203],{"id":202},"ev-中期环氧树脂","EV 中期：环氧树脂",[21,205,207],{"id":206},"环氧a-两批b-两批c-一批","环氧：A 两批、B 两批、C 一批",[12,209,210],{},[32,211,212],{},"用现有苯和丙烯，按 A 两批→B 两批→C 一批做首桶环氧。",[37,214,215,227],{},[40,216,217],{},[43,218,219,222,225],{},[46,220,221],{},"工序",[46,223,224],{},"LCR 配方",[46,226,57],{},[59,228,229,240,251],{},[43,230,231,234,237],{},[64,232,233],{},"A，电路 24",[64,235,236],{},"1000 L 丙烯 + 1000 L 苯 + 100 L 磷酸 + 2000 L 氧 → 1000 L 苯酚 + 1000 L 丙酮",[64,238,239],{},"30 EU\u002Ft，24 秒",[43,241,242,245,248],{},[64,243,244],{},"B，电路 23",[64,246,247],{},"3 氢氧化钠粉 + 1000 L 丙烯 + 4000 L 氯 + 1000 L 水 → 1000 L 环氧氯丙烷 + 1000 L 盐水 + 2000 L 盐酸",[64,249,250],{},"30 EU\u002Ft，32 秒",[43,252,253,256,259],{},[64,254,255],{},"C，电路 24",[64,257,258],{},"6 氢氧化钠粉 + 1000 L 丙酮 + 2000 L 苯酚 + 1000 L 盐酸 + 2000 L 环氧氯丙烷 → 1000 L 环氧树脂 + 2000 L 盐水",[64,260,239],{},[12,262,263],{},"一轮产 1000 L 环氧，净余 1000 L 丙酮、3000 L 盐酸、4000 L 盐水，分别留罐。每轮补 200 L 磷酸；已有木焦油苯酚时，可以少做 A，但要另备 C 所需的丙酮。",[12,265,266,267],{},"第一批可以共用一台 LCR，按 A→B→C 清空并切换；常驻生产再拆为专机。C 的四种输入流体分别安排独立输入仓。",[126,268,270],{"href":128,"rel":269},[130],"RC-2 环氧配方",[12,272,273,274,279],{},"中文工艺对照：",[126,275,278],{"href":276,"rel":277},"https:\u002F\u002Fgtnh.huijiwiki.com\u002Fwiki\u002F%E7%8E%AF%E6%B0%A7%E6%A0%91%E8%84%82",[130],"环氧树脂：双酚 A、丙烯与甘油分支","。本节 A\u002FB\u002FC 表使用 LCR 合并路线。",[21,281,283],{"id":282},"环氧开工前一份-1000-l-成品的物料账","环氧开工前：一份 1000 L 成品的物料账",[12,285,286,287,290],{},"首桶备 ",[152,288,289],{},"4000 L 丙烯、2000 L 苯、200 L 磷酸、4000 L 氧、8000 L 氯、2000 L 水、12 氢氧化钠粉","。A 两批、B 两批后再做 C；C 所需盐酸直接取 B 的副产。",[292,293,295],"collapse",{"title":294},"查看每批产物和去向",[37,296,297,310],{},[40,298,299],{},[43,300,301,304,307],{},[46,302,303],{},"批次阶段",[46,305,306],{},"应看到的关键库存",[46,308,309],{},"下一步",[59,311,312,323,334],{},[43,313,314,317,320],{},[64,315,316],{},"A 做两次",[64,318,319],{},"苯酚 2000 L、丙酮 2000 L",[64,321,322],{},"保留其中 1000 L 丙酮作余量",[43,324,325,328,331],{},[64,326,327],{},"B 做两次",[64,329,330],{},"环氧氯丙烷 2000 L、盐酸 4000 L、盐水 2000 L",[64,332,333],{},"给 C 留 1000 L 盐酸",[43,335,336,339,342],{},[64,337,338],{},"C 做一次",[64,340,341],{},"环氧树脂 1000 L，新增盐水 2000 L",[64,343,344],{},"收成品，保留余丙酮\u002F盐酸",[12,346,347,350],{},[32,348,349],{},"盐水按每桶环氧净增 4000 L 留出口。"," 16000 L 盐水罐四轮就满，连续线接回收或库存控制。",[16,352,353],{"id":353},"接下来读什么",[355,356,357,364,370,376],"ul",{},[358,359,360],"li",{},[126,361,363],{"href":362},"\u002Fblog\u002Fgtnh\u002Fpolyethylene","聚乙烯产线",[358,365,366],{},[126,367,369],{"href":368},"\u002Fblog\u002Fgtnh\u002Ftitanium","钛的首批生产与回收",[358,371,372],{},[126,373,375],{"href":374},"\u002Fblog\u002Fgtnh\u002Fae2","AE2 自动合成",[358,377,378,382,383],{},[126,379,381],{"href":380},"\u002Fblog\u002Fgtnh\u002Fhv","主线：HV 阶段"," · ",[126,384,386],{"href":385},"\u002Fblog\u002Fgtnh\u002Fev","主线：EV 阶段",{"title":388,"searchDepth":389,"depth":389,"links":390},"",2,[391,396,400,404],{"id":18,"depth":389,"text":19,"children":392},[393,395],{"id":23,"depth":394,"text":24},3,{"id":137,"depth":394,"text":138},{"id":174,"depth":389,"text":175,"children":397},[398,399],{"id":178,"depth":394,"text":179},{"id":191,"depth":394,"text":192},{"id":202,"depth":389,"text":203,"children":401},[402,403],{"id":206,"depth":394,"text":207},{"id":282,"depth":394,"text":283},{"id":353,"depth":389,"text":353},"games",null,"2026-10-29","先用 MV 小化反解开 PTFE 与 LCR 的前置，再逐步升级合并反应、硅橡胶和 EV 环氧的整批物料。","md",[],{},true,"\u002Fblog\u002Fgtnh\u002Fadvanced-chemistry",{"title":5,"description":408},"blog\u002Fgtnh\u002Fadvanced-chemistry",[6,417,418],"guide","minecraft","rufFIloug3ErDv6aqH9cLnZYgTxfFF37b1RiROmFDRs",{"newer":406,"older":406,"related":421},[],1793292207799]