Foreword
This system is extremely dependent onrequestorThe requestor has a bug in version 0.5.6beta. A master developer has created a bug fix mod, and you can get a better experience by using this mod together. It can be downloaded from the GTO community group.
However, in my own completion process, I used a buggy requester. It could complete 80% of the orders, and for 20% of the materials, it wouldn't place orders at all. I relied on manually placing more orders at once to get me through the entire process.
This tutorial is a foolproof plan. You only need to follow the settings for the marker materials of each machine, and you need to write some boilerplate yourself. I will specifically indicate when a recipe needs to be specified.It may lead to the loss of some game fun (or gain?)
Suggest searching for GTOcore in the mod settings within the game's settings; changing the default minimum overclocking time to 1 tick will set the default minimum overclocking time for all placed machines to 1 tick. The specific mechanism is complex to explain, but in terms of effect, this can increase the operating speed of under-parallelized chemical plants by 2-16 times. Furthermore, modifying this configuration will only benefit power saving and acceleration, and will not cause any machines to consume more power or run slower.
Platinum treatment
MaterialsLarge baler, large chemical leaching machine, large distillation column, chemical plant, large mixing tank, vacuum drying oven, large electrolytic cell, cracking machine, large screening funnel, large centrifuge, reactor (with module), general factory + HV fluid curer, 9 IV acceleration bays, 9 LUV parallel bays
The scheme does not require a sample assembly and sample input assembly, of course, it's better to have them, but considering that the time between the chemical plant and the sample assembly is not short.
This production lineconsumes: toner, hydrogen, oxygen, nitrogen, chlorine, steam, sulfur powder, sodium hydroxide, nitric acid, hydrochloric acid, purified Sheldon ore (other types are also acceptable, or all of them)
This production lineInternal loop : Calcium powder, zinc powder, potassium powder (tested, when the chemical plant continuously processes multiple formulations in a certain group of inputs, the reaction of crude platinum powder and calcium may lose products, leading to less calcium powder.) (Although it can self-cycle, these powders are very common, it is recommended to pull directly from the main grid)
This production lineproduces : silica powder, sodium powder, salt, platinum, palladium, ruthenium, iridium, osmium, rhodium, gold, nickel, sulfuric acid, ammonia
Baler: Small pinch of inert metal mixture; Small pinch of rare metal mixture
Chemical washing machine: osmium oxide metal powder; sulfuric acid
Distillation Room 1 Circuit: Rhodium cake solution; dilute sulfuric acid (remember to open chamber isolation)
Distillation Chamber 2 circuit: Hot ruthenium tetroxide; acidic osmium solution; dilute hydrochloric acid (remember to open chamber isolation)
Blender: Rhodium salt powder; Rhodium filter cake powder; Water
Dehydrator: rhodium sulfate; zinc powder
Fluid hardener: Ruthenium tetroxide solution
Electrolyzer: Calcium chloride powder; Sodium sulfate powder; Potassium sulfate powder; Zinc sulfate powder; Nickel sulfate solution; Carbon monoxide(Carbon monoxide is recycled in the treatment of crude palladium powder, but platinum leaching residue powder is produced. Considering that the cost of electrolysis and re-synthesis of carbon monoxide is not high, direct electrolysis is more convenient)
Cracking machine: liquid ruthenium tetroxide; steam
Screening machine: Rhodium nitrate powder
Centrifuge: Platinum-group metals slime; Platinum slime residue; Aqua regia
Chemical Reactor Group 1: Pure Sheldon Ore; Ammonium Chloride Powder; Iridium Chloride Powder; Iridium Dioxide Powder; Reprecipitated Rhodium Powder; Osmium Tetroxide Powder; Ruthenium Tetroxide Powder; Crude Palladium Powder; Crude Platinum Powder; Calcium Powder; Nitric Acid; Hydrochloric Acid; Formic Acid; Hydrogen Gas; Water; Rhodium Sulfate Gas; Acidic Iridium
Reactor Group 2: Sodium ruthenate powder; Sodium nitrate powder; Gaseous chlorine; Oxygen; Nitrogen dioxide; Rhodium salt solution
Chemical Reactor Group 3: Temporarily Vacant
Reactor: platinum slag powder; potassium pyrosulfate powder; platinum leaching slag powder; soda ash powder; rare metal compound; inert metal compound; sodium nitrate powder; crude rhodium metal powder; salt; iridium metal slag; sodium chlorate powder; oxygen; hydrochloric acid; sulfuric acid; gaseous chlorine; hydrogen
Requester request content: Aqua regia; Potassium pyrosulfate; Formic acid; Soda ash powder; Sodium nitrate powder; Nitrogen dioxide; Sodium chlorate powder; Ammonium chloride powder
These generated products do not require specified recipes; you can write your own templates. There are four points to note:
It is more power-efficient to centrifuge or distill air directly and then synthesize nitrogen dioxide, rather than centrifuging or distilling the end air.
The chemical reactor requires the largest possible programmable bay. Recipes without programming circuits also need to place an empty virtual item with Ctrl, otherwise, recipes will be mixed;
The chemical reactor and the blender's template suppliers both need to enable the blocking mode that prevents the insertion of identical templates;
The chemical reactor is likely to be bottlenecked by input speed, so replace it with a template assembly as soon as possible.
Subnet read main netStorage bus(Priority increased): Hydrogen, Oxygen, Nitrogen, Chlorine, Hydrochloric acid, Sulfuric acid, Nitric acid, Steam, Ammonia; Pure Sheldon Ore; Sodium hydroxide; Sodium powder; Sulfur powder; Salt; Calcium powder; Potassium powder; Zinc powder; Carbon powder; Programming circuit empty 1 2 3
Increase the storage bus priority, making the main network an extended inventory where subnets are prioritized for storage. Marked content is what both subnets and the main network need (like nitrogen, oxygen, hydrogen, etc.), items that only subnets need but cannot fit (like cerium-rich mixtures from rare-earth processing), and items that subnets produce but also need (like ammonia).
Subnet to Mainnet Super Interface'sOutput Bus: Platinum, Palladium, Ruthenium, Rhodium, Osmium, Iridium, Gold, Nickel; Silicon Dioxide
The items marked here are pure products. The subnet will not use the items marked here, it will only produce these items.
Main network to subnetOutput bus: Dilute sulfuric acid; Dilute hydrochloric acid (handle these two from the main network as well)
Marked here for not using the main network, only subnets are using, and it's stuff that can be stored in subnets.
Tungsten processing
Nothing much to say, very simple
Subnet to MainnetStorage Bus: New scheelite powder; lithium tungstate powder
Chemical leaching machine: Added hydrochloric acid; Wolframite powder; Lithium tungstate powder
Electrolyzer: Added lithium chloride powder; tungsten oxide powder
The processing route for tungstate powder can be decided by oneself. Using a dehydrator followed by hydrogenation reduction saves electricity but consumes hydrogen; direct electrolysis is equivalent to electrolyzing 4 barrels of water for every 1 ton of tungsten powder processed. While it appears to consume a lot of electricity, it is not much more expensive. The direct electrolysis route is chosen here.
Subnet to mainnetOutput bus: Tungsten powder; Lithium powder
Rare earth treatment + titanium treatment
Materials：On the basis of platinum processing, add dissolution tank and boiling pool(Note that both only support parallelism and do not support acceleration)
This production lineconsumes: Monazite powder, fluorocarbon lanthanum cerium ore powder, samarium concentrate, nitric acid, saltpeter powder, carbon powder, hydrogen, oxygen, apatite, sodium hydroxide
This production lineInternal circulation : None, requires quicklime as a catalyst
This production lineoutputs16 rare earth metals(The 17th, Promethium (PM), pronounced pǒ, requires a rare earth centrifuge to produce)Silicon Dioxide, Potassium, Aluminum, Silicon, Thorium, Wrought Iron Ingot, Titanium Tetrachloride, Zirconium Powder, Uranium 235 Powder, Chloromethane, Gaseous Fluorine(Originally a small consumption item, but electrolysis of fluorocerate ore powder produces a large amount of fluorine, so it has become an output)
Note, can also pull ilmenite powder, rutile powder, bauxite powder from the main network(Not recommended, bauxite can be used to make ceramic sheets for plastic circuit boards), perform titanium treatment
This tutorial uses the processing route ofmonazite processing, with two enrichments using cerium-rich concentrate and samarium concentrate
Monazite ore, fluorocarbon lanthanum cerium ore, and neodymium ore (samarium concentrate) are associated. Each of them can produce rare earth elements through its own processing. However, only monazite processing can simultaneously consume the other two and increase production. Processing monazite is equivalent to processing all of them.
不过需要注意: 独居石可以通过高压釜12倍增产, 这会导致独居石粉远远多于另外两种矿粉的产出, 如果遇到了两种矿粉原料不足的问题, 可以考虑在搅拌机处将浓缩独居石稀土氢氧化物粉(对应氟碳镧铈矿)或独居石罕土沉淀粉(对应钐精粉)的处理改为非增产配方, 这样会消耗更多的处理耗材, 但是能完全处理掉所有独居石粉。不过大部分时间处理瓶颈不在缺失钐精粉和氟碳镧铈矿，而是煮解池效率不足。
Vacuum drying ovens and large Buchner funnels: upgrade the voltage as much as possible to increase output.
The boiling and dissolving tanks do not need to be upgraded in parallel, but the energy storage tank needs to be upgraded to improve power supply.
Packing machine: No new additions
Chemical leaching machine: Based on platinum treatment, add uranium filter residue powder; Hydrofluoric acid
Distillation column: No additions
Chemical Reactor Group 1: New rare earth hydroxide
Chemical Reactor Group 2: Add carbon powder, rutile powder
Chemical reactor group three: still vacant
Chemistry
Blender: Add concentrated monazite rare earth hydroxide powder; cerium-rich mixed powder; monazite rare earth precipitate powder; samarium concentrate powder; nitric acid; acetone; Set Circuit 2
Centrifuge: Added Lanthanum-Neodymium oxide solution; Samarium-Gadolinium oxide solution; Terbium-Holmium oxide solution; Erbium-Lutetium oxide solution
Electrolyzer: Added Carbon Dioxide; Thorium Powder; Safflower Granite Powder; Potassium Feldspar Powder; Fluorocarbon Lanthanum Cerium Ore Powder; Apatite Powder; Phosphate Powder
Fluid Curing Agent: No additions
Cracking unit: no additions
Centrifuge new programmable chamber (Thermic Centrifuge): Input Thorium Phosphate Concentrate into it using the output bus
Centrifuge: Added red zircon powder; Saturated monazite rare earth powder; HV item magnet; Rare earth chloride
Screening machine: New addition of monazite powder (acidic); samarium precipitate powder; dilute monazite rare earth slurry; monazite nitrate leach mixture
Reactor: Added sixteen rare earth metal oxides powder; Ilmenite powder; Carbon powder
Boiling tank: Input nitric acid; Monazite powder
Dissolution Tank: Since the dissolution tank module requires a logistic sorter to produce, which comes much later in the game, we complete the dissolution tank passively by using an inventory input bus/buffer + pattern provider + Applied Energistics 2: order + requester.
Use the Miaomiao Tool: Order to replace all output items in the template. The items in the order are arbitrary. I put buckets in for ease of understanding.
Then, in the requestor, mark the desired number of parallel requests. It doesn't matter if you mark too many, as there will be no imbalance. If the requestor is not working well, you can directly place 10,000 orders for missing synthesis, and raw materials will be automatically dispatched as they arrive.
The dissolution tank needs to process two recipes, which are the recipes corresponding to the two products of rare earth hydroxide and diluted monazite rare earth slurry.
Requester Add: Two Orders; Hydrofluoric Acid; Acetone(Carbon Monoxide & Hydrogen Synthesis of Acetic Acid(Faster than direct synthesis with carbon powder and hydrogen), Acetic acid becomes acetone in circuit 24 and with quicklime catalyst. Only circuit 24 is kept for virtual items in the acetone template. Since the template assembly could only send one virtual item before, place quicklime in the programmable slot of the chemical reactor. Reactors related to quicklime require at least two quicklime powders. Therefore, placing one will ensure it's not mixed up); Phosphoric Acid(Use the Phosphorus -> Phosphorus Pentoxide -> Phosphoric Acid path. This is more versatile and better utilizes other products from apatite electrolysis)
Subnet to main networkStorage bus: New Monazite powder; Bastnaesite powder; Cerium-rich mixture(Subnet can't hold it, put it in the main network); Nitre powder; Samarium concentrate powder; Apatite powder; Phosphorus powder; Gaseous fluorine; Rutile powder; Ilmenite powder (also process the main network's titanium ore)
Subnet to MainnetOutput Bus:Thorium powder; Silicon powder; Wrought iron ingot; Titanium tetrachloride; Aluminum powder; Zircon sand powder; Uranium-235 powder; Chloromethane; 16 types of rare earth metal powders
Mainnet to subnetOutput bus: No additions
Quartzite processing
⚠️ Silica processing is extremely power-hungry, please power the chemical plant and reactor to at least 64A LuV.
Siliceous rock treatment has three parts:
①: Silicon dioxide rock mixture->Low-purity silicon dioxide rock emulsion->Silicon dioxide rock powder (target product) + Low-purity silicon dioxide rock solution
②: Low-purity quartz solution->A complete processing flow->Enriched quartz powder + a very small amount of Kajin and Super Quartz
③: Enriched chert powder -> Zhengchang one processing flow -> Large amount of super energy chert powder (intended product) + Large amount of Kairen powder (intended product)
As the byproduct of siliceous rock ore can directly produce enriched siliceous rock powder, while the treatment process of low-purity siliceous rock solution is too long, consumes too much material, and has too low yield.
Suggest directly feeding low-purity silicon rock solution into the trash can for disposal
①③ Materials for Production Lines: Added Neutron Activator, Height 40, using two LUV neutron accelerators, with one Machine Control Overlay and one LUV Wireless Energy Overlay attached to each neutron accelerator, using IV Parallel Crate, set parallelism to 4, note that the output assembly can only be placed below, and the input bus of the input crate can only be placed above(Data sourced fromNeutron Activator Optimal Configuration Calculation · gtowiki)
This production lineconsumes: silica rock mixture powder; enriched silica rock powder; hydrogen; fluorine; xenon; radon; oxygen; nitrogen; cesium;
This production lineInternal loop：Cesium(Requires chemical immersion machine to reach LuV voltage, and it may still slowly decrease in actual measurement)'; The rest is not important
This production lineproduces : Silisand powder; Thermo-super Silisand ingot; Thermo-Kai-gold ingot; Thermo-enriched Silisand ingot; Thermo-titanium ingot; Indium powder; Barium powder
First, let's look at①product line:
Subnet to MainnetStorage BusNew silicon dioxide rock mixture; antimony powder
Write antimony powder -> antimony trioxide -> antimony trifluoride -> fluoroantimonic acid template, request request fluoroantimonic acid
Reactor: Added fluoroantimonic acid; silicon dioxide rock mixture; titanium trifluoride powder
Blender group 2: add sodium hydroxide; low purity silica fume emulsion (Sodium hydroxide reacts with water in group 1 under circuit 2, group 1 meets the conditions)
Subnet to MainnetOutput Bus: Silicate powder; Hot titanium ingot
Due to the large amount of siliceous rock mixture, it is necessary to stop the processing of the siliceous rock mixture in the reaction furnace after the siliceous rock powder is sufficient, so as to prevent the excessive consumption of antimony powder.
Let's look again③Production line number:
Neutron activator: Input enriched silicon rock powder; fluoroantimonic acid, neutron sensor value is 460-480
Baler: Added a pinch of super-sulfur silicon rock powder
Chemical washing machine: New sodium powder; Cesium difluorosulfate super silicon rock acid
Distillation Tower: Add a programmable slot, set to Distillation Tower mode, use ME output bus to input Supercritical Silicon Slag and Enriched Silicon Slag
First two sets of chemical reactors: no change
Chemical reactor group 3: Hyper-energetic silicon rock solution containing impurities; gaseous fluorine; hyper-energetic silicon rock hexafluoride solution; radon difluoride; radon hyper-energetic silicon rock octafluoride acid; cesium difluorooxyxenate; cesium hyper-energetic silicon rock nonafluoroxenate; nitryl fluoride (Actually, it's just several connected recipes put together)
Blender group 1: No change
Blender Group 2: Add sulfuric acid; Super silicon rock solution; Enriched silicon rock solution; Cesium difluoro super silicon rock acid
Electrolyzer: Added sodium fluoride powder; zinc sulfide powder; barium sulfide powder; radon trioxide; nitrosyl octafluoroxenate
Centrifuge: Added Acidic Super-Silica Rock Solution; Acidic Enriched Silica Rock Solution
Reactor: New additions of Sulfuric Super-silica Powder; Sulfuric Enriched Silica Powder; Sulfided Lead Powder; Zinc Powder
Requester: Request fluorantimonic acid; radon difluoride; cesium trifluoroxenate; nitryl fluoride
Subnet to MainnetStorage bus: New enriched diatomaceous earth powder; Silicon-diatomaceous earth mixture; Antimony powder; Gaseous radon; Gaseous xenon
Subnet to Mainnet Output Bus: Hot Titanium Ingots; Silicon Rock Powder; Indium Powder; Hot Super Silicon Rock Ingots; Hot Kaijin Ingots; Hot Enriched Silicon Rock Ingots; Barium Powder
Afterword
To this end, we have completed the processing of three difficult production lines + two simple production lines with one set of machinery.
In fact, it is clearly visible that there are still vacancies in facilities such as chemical plants that can be input, and we can obviously continue to put in methods such as zircon processing and francium processing.
Not to mention that withthe template configuration input assemblyandthe template assemblywe can utilize the chemical plant's production capacity almost without limit.
But because these processing periods are too late, it is very likely that it is time to replace platinum processing with nano-integration processing.
Once platinum processing is removed from this processing system, it is very simple to insert another processing system.
So the integration after that won't be included in the tutorial.