[{"data":1,"prerenderedAt":561},["ShallowReactive",2],{"\u002Fblog\u002Fgtnh\u002Fplatinum":3,"article-navigation:\u002Fblog\u002Fgtnh\u002Fplatinum":559},{"id":4,"title":5,"album":6,"albumIndex":7,"body":8,"category":544,"cover":545,"coverAlt":545,"coverCaption":545,"date":546,"description":547,"draft":7,"extension":548,"home":7,"homeFacts":549,"homeImage":545,"homeNote":545,"meta":550,"navigation":551,"path":552,"seo":553,"stem":554,"tags":555,"updated":545,"__hash__":558},"blog\u002Fblog\u002Fgtnh\u002Fplatinum.md","铂系处理：首批铂、铂渣与铱锇分支","gtnh",false,{"type":9,"value":10,"toc":524},"minimark",[11,15,20,27,30,103,113,117,121,132,143,146,229,242,249,252,262,265,269,272,275,279,290,300,313,316,320,323,371,374,378,405,408,412,422,429,433,440,447,461,464,482,506,509],[12,13,14],"p",{},"EV 先产铂供电路，IV 接铂渣、铱和其他金属分支。各分支先做出升级机器所需的材料，再把频繁使用的工序专机化。",[16,17,19],"h2",{"id":18},"开工前准备这些接口","开工前：准备这些接口",[12,21,22,26],{},[23,24,25],"strong",{},"先做铂，再接铱。"," 复用 LCR、高炉、筛选机；备铂金属粉、盐酸、硝酸、氨、钙。浓缩液、钯液、返酸、二氧化氮、循环粉与铂渣分别留出口。",[12,28,29],{},"物品箱按下表标名，循环粉和纯铂分开：",[31,32,33,46],"table",{},[34,35,36],"thead",{},[37,38,39,43],"tr",{},[40,41,42],"th",{},"材料",[40,44,45],{},"本文用途",[47,48,49,62,73,84,92],"tbody",{},[37,50,51,59],{},[52,53,54,55],"td",{},"铂金属粉 ",[56,57,58],"code",{},"Platinum Metallic Powder",[52,60,61],{},"投入提纯、由精制盐回收；保留循环库存",[37,63,64,70],{},[52,65,66,67],{},"粗制铂粉 ",[56,68,69],{},"Platinum Raw Powder",[52,71,72],{},"加钙反应，得到可用铂粉",[37,74,75,81],{},[52,76,77,78],{},"铂粉 ",[56,79,80],{},"Platinum Dust",[52,82,83],{},"最终金属原料，进入冶炼和细线加工",[37,85,86,89],{},[52,87,88],{},"粗制／精制铂盐",[52,90,91],{},"筛选与高炉回流中的中间物",[37,93,94,100],{},[52,95,96,97],{},"铂渣 ",[56,98,99],{},"Platinum Residue",[52,101,102],{},"后续铑、钌、锇、铱分支的入口",[12,104,105,106],{},"以下时间、功率为原始配方值。 ",[107,108,112],"a",{"href":109,"rel":110},"https:\u002F\u002Fgithub.com\u002FGTNewHorizons\u002FGT5-Unofficial\u002Fblob\u002F5.09.54.205\u002Fsrc\u002Fmain\u002Fjava\u002Fbartworks\u002Fsystem\u002Fmaterial\u002Fgtenhancement\u002FPlatinumSludgeRecipes.java",[111],"nofollow","GT5 5.09.54.205 铂系配方",[16,114,116],{"id":115},"首批铂以-9-份铂金属粉为一轮","首批铂：以 9 份铂金属粉为一轮",[118,119,120],"h3",{"id":120},"先制王水与氯化铵",[12,122,123,124,127,128,131],{},"王水使用 ",[56,125,126],{},"3000 L 盐酸＋1000 L 硝酸 → 4000 L 王水","。普通搅拌机可选电路 3：输入一格硝酸单元和液态盐酸，输出 4000 L 王水与一个空单元，",[56,129,130],{},"30 EU\u002Ft、1.5 秒","。选用其他单元形式时连同电路一起更换。",[12,133,134,135,138,139,142],{},"氯化铵由等体积氨与盐酸制取。LCR 批量配方为电路 9：",[56,136,137],{},"64000 L 氨＋64000 L 盐酸 → 64000 L 氯化铵","，",[56,140,141],{},"480 EU\u002Ft、3 秒","；启动库存少时可先用普通小配方逐批积攒。",[118,144,145],{"id":145},"一轮实际怎么接",[31,147,148,161],{},[34,149,150],{},[37,151,152,155,158],{},[40,153,154],{},"步骤",[40,156,157],{},"选用配方",[40,159,160],{},"原始条件",[47,162,163,174,185,196,207,218],{},[37,164,165,168,171],{},[52,166,167],{},"1. 溶解",[52,169,170],{},"9 铂金属粉＋18000 L 王水 → 18000 L 铂浓缩液＋1 铂渣；电路 9",[52,172,173],{},"化反／LCR，30 EU\u002Ft、112.5 秒",[37,175,176,179,182],{},[52,177,178],{},"2. 分离",[52,180,181],{},"4000 L 铂浓缩液＋400 L 氯化铵 → 16 小撮粗制铂盐＋4 小撮粗制铂粉＋400 L 钯富氨液＋1000 L 二氧化氮＋3000 L 盐酸；电路 1",[52,183,184],{},"LCR，30 EU\u002Ft、64 秒",[37,186,187,190,193],{},[52,188,189],{},"3. 汇整",[52,191,192],{},"小撮粉按 9:1 合并为整粉；分别积攒粗制铂盐与粗制铂粉",[52,194,195],{},"保留两条输出",[37,197,198,201,204],{},[52,199,200],{},"4. 筛选",[52,202,203],{},"1 粗制铂盐 → 多格概率产出的精制铂盐",[52,205,206],{},"筛选机，30 EU\u002Ft、30 秒",[37,208,209,212,215],{},[52,210,211],{},"5. 循环",[52,213,214],{},"1 精制铂盐 → 1 铂金属粉＋87 L 氯；电路 1",[52,216,217],{},"高炉，900 K、120 EU\u002Ft、10 秒",[37,219,220,223,226],{},[52,221,222],{},"6. 成品",[52,224,225],{},"4 粗制铂粉＋1 钙粉 → 2 铂粉＋3 氯化钙粉",[52,227,228],{},"化反／LCR，30 EU\u002Ft、1.5 秒",[12,230,231,232,235,236,241],{},"第一轮 18000 L 浓缩液只能完成四批步骤 2，余 2000 L 留罐；产出 16 小撮粗制铂粉，还不足四整粉。",[23,233,234],{},"首批按三轮步骤 1 备料：27 铂金属粉、54000 L 王水、5200 L 氯化铵和 1 钙粉。"," 得到的 54000 L 浓缩液可完成 13 批步骤 2，产出 52 小撮粗制铂粉，合并后做出首批 2 铂粉；余料留待下一批。",[107,237,240],{"href":238,"rel":239},"https:\u002F\u002Fgithub.com\u002FGTNewHorizons\u002FGT5-Unofficial\u002Fblob\u002F5.09.54.205\u002Fsrc\u002Fmain\u002Fjava\u002Fbartworks\u002Fsystem\u002Fmaterial\u002Fgtenhancement\u002FPlatinumSludgeRecipes.java#L309-L393",[111],"溶解与分离配方","。",[12,243,244,245,248],{},"筛选每次平均返 0.95 精制铂盐。返还的铂金属粉回溶解，纯铂走成品出口。循环粉暂时凑不齐 9 份时，可用电路 1：",[56,246,247],{},"1 铂金属粉＋2000 L 王水 → 2000 L 浓缩液＋1 小撮铂渣","，30 EU\u002Ft、12.5 秒；攒齐后再用九份批量配方。",[118,250,251],{"id":251},"为什么首批与量产采用不同批量",[12,253,254,257,258,261],{},[23,255,256],{},"量产改 LCR 电路 3："," ",[56,259,260],{},"36000 L 铂浓缩液＋3600 L 氯化铵→16 粗制铂盐＋4 粗制铂粉＋3600 L 钯富氨液＋9000 L 二氧化氮＋27000 L 盐酸","，480 EU\u002Ft、35 秒，直接出整粉。",[12,263,264],{},"9 粉溶解跑两轮，凑 36000 L 浓缩液，再做上面一批；所有副产接好出口后连续进料。",[118,266,268],{"id":267},"酸怎样回先保盐酸再接硝酸","酸怎样回：先保盐酸，再接硝酸",[12,270,271],{},"每消耗 4000 L 王水形成的浓缩液，分离返还 3000 L 盐酸和 1000 L 二氧化氮。盐酸直接回王水；二氧化氮送回现有硝酸线，以所选硝酸配方补足水、氧等输入。分离出口优先送回流罐，回流罐有余量后才供其他化工。",[12,273,274],{},"启动时外备王水、氯化铵和循环粉。氯化铵持续消耗氨和盐酸，观察这两罐的存量，下降时补充原料。",[16,276,278],{"id":277},"钯处理铂线持续产出的富氨液","钯：处理铂线持续产出的富氨液",[12,280,281,282,285,286,289],{},"初次可用电路 2：",[56,283,284],{},"1000 L 钯富氨液 → 1 钯盐","，化反／LCR 原始 ",[56,287,288],{},"30 EU\u002Ft、12.5 秒","。筛选钯盐返回钯金属粉，有库存后切换为循环配方：",[291,292,298],"pre",{"className":293,"code":295,"language":296,"meta":297},[294],"language-text","9 钯金属粉＋9000 L 钯富氨液\n→ 16 钯盐＋2 粗制钯粉\n","text","",[56,299,295],{"__ignoreMap":297},[12,301,302,303,306,307,138,310,312],{},"这是电路 9、",[56,304,305],{},"30 EU\u002Ft、112.5 秒","。钯盐继续筛选，筛出的钯金属粉留作循环；粗制钯粉进入成品处理。LCR 的成品配方为 ",[56,308,309],{},"4 粗制钯粉＋4000 L 甲酸 → 2 钯粉＋4000 L 氨＋1000 L 乙烯＋1000 L 水",[56,311,288],{},"。氨返回氯化铵／钯循环相关工序，乙烯接塑料或单独存罐。",[12,314,315],{},"甲酸的前端可复用一氧化碳和氢氧化钠：先制甲酸钠，再以硫酸酸化；副产硫酸钠保留。先打通一批甲酸与钯成品，再放开富氨液的自动进料。",[16,317,319],{"id":318},"铂渣先拆出铱和锇的入口","铂渣：先拆出铱和锇的入口",[118,321,322],{"id":322},"共用前段按这个批量运行",[31,324,325,337],{},[34,326,327],{},[37,328,329,331,334],{},[40,330,154],{},[40,332,333],{},"输入 → 输出",[40,335,336],{},"条件",[47,338,339,350,360],{},[37,340,341,344,347],{},[52,342,343],{},"分铑",[52,345,346],{},"1 铂渣＋360 L 熔融焦硫酸钾 → 1 浸出渣＋360 L 硫酸铑；电路 11",[52,348,349],{},"高炉，775 K、120 EU\u002Ft、10 秒",[37,351,352,355,358],{},[52,353,354],{},"分钌",[52,356,357],{},"10 浸出渣＋10 硝石粉＋1000 L 盐水 → 3 钌酸钠＋6 铱锇浸出渣＋1000 L 蒸汽",[52,359,349],{},[37,361,362,365,368],{},[52,363,364],{},"分锇",[52,366,367],{},"2 铱锇浸出渣＋500 L 盐酸 → 1 铱浸出渣＋1000 L 酸性锇溶液；电路 11",[52,369,370],{},"高炉，775 K、120 EU\u002Ft、5 秒",[12,372,373],{},"这一组需要先凑十份浸出渣，再把得到的六份铱锇渣分三次处理；得到三份铱浸出渣、3000 L 酸性锇溶液。硫酸铑与钌酸钠先各自入缓存，优先继续铱分支。",[118,375,377],{"id":376},"铱首批优先做关键升级","铱：首批优先做关键升级",[379,380,381,388,394,399],"ol",{},[382,383,384,387],"li",{},[56,385,386],{},"1 铱浸出渣 → 1 二氧化铱＋1 残渣","，高炉电路 1，775 K、120 EU\u002Ft、10 秒。",[382,389,390,393],{},[56,391,392],{},"1 二氧化铱＋1000 L 盐酸 → 1000 L 酸性铱溶液","，化反／LCR，30 EU\u002Ft、15 秒。",[382,395,396,393],{},[56,397,398],{},"1000 L 酸性铱溶液＋3000 L 氯化铵 → 1 氯化铱＋3000 L 氨",[382,400,401,404],{},[56,402,403],{},"1 氯化铱＋1 钙粉 → 1 铱粉＋1 后续残渣＋3000 L 氯化钙","，化反／LCR，1920 EU\u002Ft、15 秒。",[12,406,407],{},"首批铱先做 IV 能源仓和关键设备；氨回氯化铵线，残渣留箱，氯化钙粉／流体分别收。",[118,409,411],{"id":410},"锇iv-蒸馏是这一支的门槛","锇：IV 蒸馏是这一支的门槛",[12,413,414,417,418,421],{},[56,415,416],{},"1000 L 酸性锇溶液 → 100 L 锇溶液＋900 L 水","，蒸馏塔原始 ",[23,419,420],{},"7680 EU\u002Ft、7.5 秒","。至少处理十批才能得到后续一批所需的 1000 L 锇溶液。",[12,423,424,425,428],{},"后续 ",[56,426,427],{},"1000 L 锇溶液＋6000 L 盐酸 → 1 锇粉＋7000 L 氯＋2000 L 水","，化反／LCR，30 EU\u002Ft、15 秒。前述一组十份铂渣仅得到 3000 L 酸性锇溶液，先把这份中间液存好，积攒至十桶再集中蒸馏。",[16,430,432],{"id":431},"钌与铑按合金订单打开分支","钌与铑：按合金订单打开分支",[12,434,435,436,439],{},"钌的主线为：",[23,437,438],{},"钌酸钠加氯 → 四氧化钌溶液 → 流体加热 → 热四氧化钌溶液 → 蒸馏 → 四氧化钌 → 钌粉","。其中 1000 L 普通溶液加热得到 2000 L 热溶液；蒸馏按 9000 L 热溶液一批，给出 7200 L 四氧化钌、1800 L 水与 6 盐粉，原始 480 EU\u002Ft、75 秒。四氧化钌先固化为粉，再以盐酸还原，氯回前段。",[12,441,442,443,446],{},"铑的主线为：",[23,444,445],{},"硫酸铑稀释与回钾 → 锌置换得粗铑 → 加盐与氯制铑盐 → 溶水 → 硝酸钠处理 → 筛出滤饼 → 溶水与再处理 → 盐酸处理得铑","。先按 NEI 手动跑通一轮，把返还的钾、氨、氯和硫酸锌分开存放，再接入对应回路。",[12,448,449,450,455,456,241],{},"钌铱合金（Ruridit）细线是 LuV 马达材料之一；规划装配线时同步安排钌和铱的订单。钌、铑的完整工序可对照",[107,451,454],{"href":452,"rel":453},"https:\u002F\u002Fgtnh.huijiwiki.com\u002Fwiki\u002F%E9%93%82%E5%A4%84%E7%90%86\u002F%E9%92%8C",[111],"中文钌分支","和",[107,457,460],{"href":458,"rel":459},"https:\u002F\u002Fgtnh.huijiwiki.com\u002Fwiki\u002F%E9%93%82%E5%A4%84%E7%90%86\u002F%E9%93%91",[111],"中文铑分支",[16,462,463],{"id":463},"小技巧与排障",[465,466,467,470,473,476,479],"ul",{},[382,468,469],{},"小撮粉九份合一整粉，样板分别记两种数量。",[382,471,472],{},"循环粉先回原线，纯金属进公共仓库。",[382,474,475],{},"共用 LCR 一次发一单，清空余料余液后切换。",[382,477,478],{},"成品不涨，从末端往前找缺料；锇先凑十批蒸馏。",[382,480,481],{},"停机先清满罐、满总线，再补输入。",[12,483,484,485,490,491,490,496,490,501,241],{},"延伸阅读：",[107,486,489],{"href":487,"rel":488},"https:\u002F\u002Fgtnh.huijiwiki.com\u002Fwiki\u002F%E9%93%82%E5%A4%84%E7%90%86",[111],"中文铂处理总览","、",[107,492,495],{"href":493,"rel":494},"https:\u002F\u002Fgtnh.huijiwiki.com\u002Fwiki\u002F%E9%93%82%E5%A4%84%E7%90%86\u002F%E9%93%82",[111],"铂分支",[107,497,500],{"href":498,"rel":499},"https:\u002F\u002Fgtnh.huijiwiki.com\u002Fwiki\u002F%E9%93%82%E5%A4%84%E7%90%86\u002F%E9%93%82%E6%B8%A3",[111],"铂渣分支",[107,502,505],{"href":503,"rel":504},"https:\u002F\u002Fwiki.gtnewhorizons.com\u002Fwiki\u002FPlatinum_Processing_Line",[111],"国际 Wiki 铂系处理",[16,507,508],{"id":508},"接下来读什么",[12,510,511,515,516,515,520],{},[107,512,514],{"href":513},"\u002Fblog\u002Fgtnh\u002Fev","主线：EV 阶段"," · ",[107,517,519],{"href":518},"\u002Fblog\u002Fgtnh\u002Fiv","主线：IV 阶段",[107,521,523],{"href":522},"\u002Fblog\u002Fgtnh\u002Fassembly-line","装配线与首批 LuV 部件",{"title":297,"searchDepth":525,"depth":525,"links":526},2,[527,528,535,536,541,542,543],{"id":18,"depth":525,"text":19},{"id":115,"depth":525,"text":116,"children":529},[530,532,533,534],{"id":120,"depth":531,"text":120},3,{"id":145,"depth":531,"text":145},{"id":251,"depth":531,"text":251},{"id":267,"depth":531,"text":268},{"id":277,"depth":525,"text":278},{"id":318,"depth":525,"text":319,"children":537},[538,539,540],{"id":322,"depth":531,"text":322},{"id":376,"depth":531,"text":377},{"id":410,"depth":531,"text":411},{"id":431,"depth":525,"text":432},{"id":463,"depth":525,"text":463},{"id":508,"depth":525,"text":508},"games",null,"2026-10-29","分批打通铂系处理，列出铂金属粉提纯、循环粉回流、钯分支，以及从铂渣取得铱与锇的关键配方。","md",[],{},true,"\u002Fblog\u002Fgtnh\u002Fplatinum",{"title":5,"description":547},"blog\u002Fgtnh\u002Fplatinum",[6,556,557],"guide","minecraft","bQ5o6JL4aC7cxZ9daWwE2fdclYELJZRK6n5dq1Tkn24",{"newer":545,"older":545,"related":560},[],1793292208260]