Fuel and booster producer bill of materials

Each linked producer branch, selected native recipe, quantity, electrical draw, duration, throughput, feed mass balance and first-source boundary. Oil is a finite extracted resource; solar and batteries are not counted as continuous fuel generation.

PF001

Final high-octane gasoline mixer

Include; proposed producer capacity
Final high-octane gasoline mixer
Offline wiki reference / native texture

Proposed quantity

1

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
1,169
Recipe
Map
gt.recipe.largechemicalreactor
Ordinal
821
M EUt
1,920
M Duration
50
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
  • Programmed Circuit × 0 gregtech:gt.integrated_circuit @24
Outputs
None recorded
Fluid Inputs
  • Name
    gasoline
    Amount
    20,000
  • Name
    octane
    Amount
    2,000
  • Name
    nitrousoxide
    Amount
    6,000
  • Name
    liquid_toluene
    Amount
    1,000
  • Name
    ethyltertbutylether
    Amount
    3,000
Fluid Outputs
  • Name
    highoctanegasoline
    Amount
    32,000
Metadata
Voltage
512
Working Amps
4
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
1,920
Max Electrical Draw Bank EUt
1,920
Actual Duration Ticks
50
Selected Fluid
highoctanegasoline
Selected Fluid Minimum Demand MBper Second
2,560
Native Electrical Capacity MBper Second
12,800.0
Capacity Margin MBper Second
10,240.0
Stock Control Duty At Minimum Demand
0.2
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
PF002

Gasoline upgrading

Include; proposed producer capacity
Gasoline upgrading
Offline wiki reference / native texture

Proposed quantity

1

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
1,169
Recipe
Map
gt.recipe.largechemicalreactor
Ordinal
820
M EUt
480
M Duration
10
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
  • Programmed Circuit × 0 gregtech:gt.integrated_circuit @24
Outputs
None recorded
Fluid Inputs
  • Name
    rawgasoline
    Amount
    10,000
  • Name
    liquid_toluene
    Amount
    1,000
Fluid Outputs
  • Name
    gasoline
    Amount
    11,000
Metadata
Voltage
512
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
480
Max Electrical Draw Bank EUt
480
Actual Duration Ticks
10
Selected Fluid
gasoline
Selected Fluid Minimum Demand MBper Second
1,600
Native Electrical Capacity MBper Second
22,000.0
Capacity Margin MBper Second
20,400.0
Stock Control Duty At Minimum Demand
0.07272727272727272
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
PF003

Raw gasoline mixing

Include; proposed producer capacity
Raw gasoline mixing
Offline wiki reference / native texture

Proposed quantity

1

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
1,169
Recipe
Map
gt.recipe.largechemicalreactor
Ordinal
819
M EUt
480
M Duration
100
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
  • Programmed Circuit × 0 gregtech:gt.integrated_circuit @24
Outputs
None recorded
Fluid Inputs
  • Name
    liquid_naphtha
    Amount
    16,000
  • Name
    gas_gas
    Amount
    2,000
  • Name
    methanol
    Amount
    1,000
  • Name
    acetone
    Amount
    1,000
Fluid Outputs
  • Name
    rawgasoline
    Amount
    20,000
Metadata
Voltage
512
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
480
Max Electrical Draw Bank EUt
480
Actual Duration Ticks
100
Selected Fluid
rawgasoline
Selected Fluid Minimum Demand MBper Second
1,454.5454545454545
Native Electrical Capacity MBper Second
4,000.0
Capacity Margin MBper Second
2,545.4545454545455
Stock Control Duty At Minimum Demand
0.36363636363636365
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
PF004

Nitrous oxide

Include; proposed producer capacity
Nitrous oxide
Offline wiki reference / native texture

Proposed quantity

1

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
1,169
Recipe
Map
gt.recipe.largechemicalreactor
Ordinal
818
M EUt
480
M Duration
50
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
  • Programmed Circuit × 0 gregtech:gt.integrated_circuit @24
Outputs
None recorded
Fluid Inputs
  • Name
    nitrogen
    Amount
    20,000
  • Name
    oxygen
    Amount
    10,000
Fluid Outputs
  • Name
    nitrousoxide
    Amount
    10,000
Metadata
Voltage
512
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
480
Max Electrical Draw Bank EUt
480
Actual Duration Ticks
50
Selected Fluid
nitrousoxide
Selected Fluid Minimum Demand MBper Second
480
Native Electrical Capacity MBper Second
4,000.0
Capacity Margin MBper Second
3,520.0
Stock Control Duty At Minimum Demand
0.12
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
PF005

ETBE synthesis

Include; proposed producer capacity
ETBE synthesis
Offline wiki reference / native texture

Proposed quantity

6

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
1,169
Recipe
Map
gt.recipe.largechemicalreactor
Ordinal
822
M EUt
480
M Duration
400
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
  • Programmed Circuit × 0 gregtech:gt.integrated_circuit @24
Outputs
None recorded
Fluid Inputs
  • Name
    bioethanol
    Amount
    1,000
  • Name
    butene
    Amount
    1,000
Fluid Outputs
  • Name
    ethyltertbutylether
    Amount
    1,000
Metadata
Voltage
512
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
480
Max Electrical Draw Bank EUt
2,880
Actual Duration Ticks
400
Selected Fluid
ethyltertbutylether
Selected Fluid Minimum Demand MBper Second
240
Native Electrical Capacity MBper Second
300.0
Capacity Margin MBper Second
60.0
Stock Control Duty At Minimum Demand
0.8
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
Perfect Overclock Enabled
Yes
OCCount
0
PF006

Bioethanol hydration

Include; proposed producer capacity
Bioethanol hydration
Offline wiki reference / native texture

Proposed quantity

6

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
1,169
Recipe
Map
gt.recipe.largechemicalreactor
Ordinal
78
M EUt
480
M Duration
400
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
  • Programmed Circuit × 0 gregtech:gt.integrated_circuit @24
Outputs
None recorded
Fluid Inputs
  • Name
    ethylene
    Amount
    1,000
  • Name
    steam
    Amount
    2,000
Fluid Outputs
  • Name
    bioethanol
    Amount
    1,000
Metadata
Voltage
512
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
480
Max Electrical Draw Bank EUt
2,880
Actual Duration Ticks
400
Selected Fluid
bioethanol
Selected Fluid Minimum Demand MBper Second
240
Native Electrical Capacity MBper Second
300.0
Capacity Margin MBper Second
60.0
Stock Control Duty At Minimum Demand
0.8
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
Perfect Overclock Enabled
Yes
OCCount
0
PF007

Medium crude-oil fractionation

Include; proposed producer capacity
Medium crude-oil fractionation
Offline wiki reference / native texture
More reference pictures
Medium crude-oil fractionation
Offline wiki reference / native texture
Medium crude-oil fractionation
Offline wiki reference / native texture

Proposed quantity

4

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
1,126
Recipe
Map
gt.recipe.distillationtower
Ordinal
64
M EUt
480
M Duration
32
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
  • Programmed Circuit × 0 gregtech:gt.integrated_circuit @9
Outputs
None recorded
Fluid Inputs
  • Name
    liquid_medium_oil
    Amount
    1,000
Fluid Outputs
  • Name
    liquid_sulfuricheavy_fuel
    Amount
    100
  • Name
    liquid_sufluriclight_fuel
    Amount
    500
  • Name
    liquid_sulfuricnaphtha
    Amount
    1,500
  • Name
    naphthenicacid
    Amount
    25
  • Name
    gas_sulfuricgas
    Amount
    600
Metadata
Voltage
512
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
480
Max Electrical Draw Bank EUt
1,920
Actual Duration Ticks
32
Selected Fluid
liquid_sulfuricnaphtha
Selected Fluid Minimum Demand MBper Second
3,750
Native Electrical Capacity MBper Second
3,750.0
Capacity Margin MBper Second
0.0
Stock Control Duty At Minimum Demand
1.0
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
Required Crude Oil MBper Second
2,500
Five Fluid Output Hatches
One distinct ordered output per native fraction; retain sulfuric-heavy/light/naphtha, naphthenic acid and sulfuric gas.
PF008

Naphtha desulfurization

Include; proposed producer capacity
Naphtha desulfurization
Offline wiki reference / native texture

Proposed quantity

3

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
1,169
Recipe
Map
gt.recipe.largechemicalreactor
Ordinal
865
M EUt
30
M Duration
160
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
  • Programmed Circuit × 0 gregtech:gt.integrated_circuit @4
Outputs
None recorded
Fluid Inputs
  • Name
    liquid_sulfuricnaphtha
    Amount
    12,000
  • Name
    hydrogen
    Amount
    2,000
Fluid Outputs
  • Name
    liquid_naphtha
    Amount
    12,000
  • Name
    liquid_hydricsulfur
    Amount
    1,000
Metadata
Recipe Metadata Key{clazz=java.lang.Boolean, identifier=cleanroom'}
false
Voltage
32
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
30
Max Electrical Draw Bank EUt
90
Actual Duration Ticks
160
Selected Fluid
liquid_naphtha
Selected Fluid Minimum Demand MBper Second
3,750
Native Electrical Capacity MBper Second
4,500.0
Capacity Margin MBper Second
750.0
Stock Control Duty At Minimum Demand
0.8333333333333334
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
PF009

Light-fuel desulfurization

Include; proposed producer capacity
Light-fuel desulfurization
Offline wiki reference / native texture

Proposed quantity

1

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
1,169
Recipe
Map
gt.recipe.largechemicalreactor
Ordinal
866
M EUt
30
M Duration
160
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
  • Programmed Circuit × 0 gregtech:gt.integrated_circuit @4
Outputs
None recorded
Fluid Inputs
  • Name
    liquid_sufluriclight_fuel
    Amount
    12,000
  • Name
    hydrogen
    Amount
    2,000
Fluid Outputs
  • Name
    liquid_light_fuel
    Amount
    12,000
  • Name
    liquid_hydricsulfur
    Amount
    1,000
Metadata
Recipe Metadata Key{clazz=java.lang.Boolean, identifier=cleanroom'}
false
Voltage
32
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
30
Max Electrical Draw Bank EUt
30
Actual Duration Ticks
160
Selected Fluid
liquid_light_fuel
Selected Fluid Minimum Demand MBper Second
1,250
Native Electrical Capacity MBper Second
1,500.0
Capacity Margin MBper Second
250.0
Stock Control Duty At Minimum Demand
0.8333333333333334
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
PF010

Refinery-gas desulfurization

Include; proposed producer capacity
Refinery-gas desulfurization
Offline wiki reference / native texture

Proposed quantity

1

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
1,169
Recipe
Map
gt.recipe.largechemicalreactor
Ordinal
864
M EUt
30
M Duration
160
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
  • Programmed Circuit × 0 gregtech:gt.integrated_circuit @4
Outputs
None recorded
Fluid Inputs
  • Name
    gas_sulfuricgas
    Amount
    16,000
  • Name
    hydrogen
    Amount
    2,000
Fluid Outputs
  • Name
    gas_gas
    Amount
    16,000
  • Name
    liquid_hydricsulfur
    Amount
    1,000
Metadata
Recipe Metadata Key{clazz=java.lang.Boolean, identifier=cleanroom'}
false
Voltage
32
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
30
Max Electrical Draw Bank EUt
30
Actual Duration Ticks
160
Selected Fluid
gas_gas
Selected Fluid Minimum Demand MBper Second
145.45454545454547
Native Electrical Capacity MBper Second
2,000.0
Capacity Margin MBper Second
1,854.5454545454545
Stock Control Duty At Minimum Demand
0.07272727272727274
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
PF011

Light-fuel hydrocracking

Include; proposed producer capacity
Light-fuel hydrocracking
Offline wiki reference / native texture

Proposed quantity

2

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
1,160
Recipe
Map
gt.recipe.craker
Ordinal
12
M EUt
240
M Duration
20
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
  • Programmed Circuit × 0 gregtech:gt.integrated_circuit @1
Outputs
None recorded
Fluid Inputs
  • Name
    liquid_light_fuel
    Amount
    1,000
  • Name
    hydrogen
    Amount
    1,600
Fluid Outputs
  • Name
    lightlyhydrocracked.lightfuel
    Amount
    1,000
Metadata
Voltage
512
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
216
Max Electrical Draw Bank EUt
432
Actual Duration Ticks
20
Selected Fluid
lightlyhydrocracked.lightfuel
Selected Fluid Minimum Demand MBper Second
1,600
Native Electrical Capacity MBper Second
2,000.0
Capacity Margin MBper Second
400.0
Stock Control Duty At Minimum Demand
0.8
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
Coil
Cupronickel, native tier0;10%EU discount. No speed modifier or forced OC.
Coil EUExact
1 - min(0.1f*(getTier()+1),0.5f); reserve216EU/t, rounded native formula.
PF012

Octane separation

Include; proposed producer capacity
Octane separation
Offline wiki reference / native texture
More reference pictures
Octane separation
Offline wiki reference / native texture
Octane separation
Offline wiki reference / native texture

Proposed quantity

5

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
1,126
Recipe
Map
gt.recipe.distillationtower
Ordinal
140
M EUt
120
M Duration
120
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
None recorded
Outputs
None recorded
Fluid Inputs
  • Name
    lightlyhydrocracked.lightfuel
    Amount
    1,000
Fluid Outputs
  • Name
    liquid_naphtha
    Amount
    800
  • Name
    octane
    Amount
    100
  • Name
    butane
    Amount
    150
  • Name
    propane
    Amount
    200
  • Name
    ethane
    Amount
    125
  • Name
    methane
    Amount
    125
Metadata
Voltage
512
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
480
Max Electrical Draw Bank EUt
2,400
Actual Duration Ticks
60
Selected Fluid
octane
Selected Fluid Minimum Demand MBper Second
160
Native Electrical Capacity MBper Second
166.66666666666666
Capacity Margin MBper Second
6.666666666666657
Stock Control Duty At Minimum Demand
0.9600000000000001
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
Other Fraction Credit MBper Second
Liquid naphtha
1,280
Credit Use
1280naphtha feeds raw gasoline demand1163.636; explicitly retain all butane/propane/ethane/methane byproducts.
PF013

Naphtha steam cracking

Include; proposed producer capacity
Naphtha steam cracking
Offline wiki reference / native texture

Proposed quantity

3

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
1,160
Recipe
Map
gt.recipe.craker
Ordinal
9
M EUt
240
M Duration
20
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
  • Programmed Circuit × 0 gregtech:gt.integrated_circuit @1
Outputs
None recorded
Fluid Inputs
  • Name
    liquid_naphtha
    Amount
    1,000
  • Name
    steam
    Amount
    1,000
Fluid Outputs
  • Name
    lightlysteamcracked.naphtha
    Amount
    1,200
Metadata
Voltage
512
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
216
Max Electrical Draw Bank EUt
648
Actual Duration Ticks
20
Selected Fluid
lightlysteamcracked.naphtha
Selected Fluid Minimum Demand MBper Second
3,000
Native Electrical Capacity MBper Second
3,600.0
Capacity Margin MBper Second
600.0
Stock Control Duty At Minimum Demand
0.8333333333333334
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
Required Naphtha And Steam MBper Second
2,500
Coil
Cupronickel,10%EU discount
PF014

Butene/ethylene separation

Include; proposed producer capacity
Butene/ethylene separation
Offline wiki reference / native texture
More reference pictures
Butene/ethylene separation
Offline wiki reference / native texture
Butene/ethylene separation
Offline wiki reference / native texture

Proposed quantity

10

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
1,126
Recipe
Map
gt.recipe.distillationtower
Ordinal
137
M EUt
120
M Duration
120
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
None recorded
Outputs
  • Tiny Pile of Carbon Dust × 1 gregtech:gt.metaitem.01 @10
Fluid Inputs
  • Name
    lightlysteamcracked.naphtha
    Amount
    1,000
Fluid Outputs
  • Name
    liquid_heavy_fuel
    Amount
    75
  • Name
    liquid_light_fuel
    Amount
    150
  • Name
    liquid_toluene
    Amount
    40
  • Name
    benzene
    Amount
    150
  • Name
    butene
    Amount
    80
  • Name
    butadiene
    Amount
    150
  • Name
    propane
    Amount
    15
  • Name
    propene
    Amount
    200
  • Name
    ethane
    Amount
    35
  • Name
    ethylene
    Amount
    200
  • Name
    methane
    Amount
    200
Metadata
Voltage
512
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
480
Max Electrical Draw Bank EUt
4,800
Actual Duration Ticks
60
Selected Fluid
butene
Selected Fluid Minimum Demand MBper Second
240
Native Electrical Capacity MBper Second
266.6666666666667
Capacity Margin MBper Second
26.666666666666686
Stock Control Duty At Minimum Demand
0.8999999999999999
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
Actual Run Flow MBper Second
3,000
Other Fraction Credit MBper Second
Ethylene
600
Liquid toluene
120
Liquid light fuel
450
Liquid heavy fuel
225
Credit Use
600ethylene exceeds240bioethanol demand.450light fuel joins1250desulfurized light fuel to supply1600hydrocracking.120toluene reduces the separate toluene demand to105.455.225heavy fuel reduces heavy desulfurization need to38.636.
PF015

Supplemental toluene separation

Include; proposed producer capacity
Supplemental toluene separation
Offline wiki reference / native texture
More reference pictures
Supplemental toluene separation
Offline wiki reference / native texture
Supplemental toluene separation
Offline wiki reference / native texture

Proposed quantity

2

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
1,126
Recipe
Map
gt.recipe.distillationtower
Ordinal
36
M EUt
480
M Duration
120
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
None recorded
Outputs
None recorded
Fluid Inputs
  • Name
    liquid_heavy_fuel
    Amount
    1,000
Fluid Outputs
  • Name
    liquid_toluene
    Amount
    400
  • Name
    benzene
    Amount
    400
  • Name
    phenol
    Amount
    250
Metadata
Voltage
512
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
480
Max Electrical Draw Bank EUt
960
Actual Duration Ticks
120
Selected Fluid
liquid_toluene
Selected Fluid Minimum Demand MBper Second
105.45454545454547
Native Electrical Capacity MBper Second
133.33333333333334
Capacity Margin MBper Second
27.878787878787875
Stock Control Duty At Minimum Demand
0.7909090909090909
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
Required Heavy Fuel MBper Second
263.6363636363636
PF016

Wood-vinegar fractionation

Include; proposed producer capacity
Wood-vinegar fractionation
Offline wiki reference / native texture
More reference pictures
Wood-vinegar fractionation
Offline wiki reference / native texture
Wood-vinegar fractionation
Offline wiki reference / native texture

Proposed quantity

2

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
1,126
Recipe
Map
gt.recipe.distillationtower
Ordinal
74
M EUt
256
M Duration
40
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
  • Programmed Circuit × 0 gregtech:gt.integrated_circuit @1
Outputs
None recorded
Fluid Inputs
  • Name
    woodvinegar
    Amount
    1,000
Fluid Outputs
  • Name
    aceticacid
    Amount
    100
  • Name
    water
    Amount
    500
  • Name
    bioethanol
    Amount
    10
  • Name
    methanol
    Amount
    300
  • Name
    acetone
    Amount
    50
  • Name
    methylacetate
    Amount
    10
Metadata
Voltage
512
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
256
Max Electrical Draw Bank EUt
512
Actual Duration Ticks
40
Selected Fluid
acetone
Selected Fluid Minimum Demand MBper Second
36.36363636363637
Native Electrical Capacity MBper Second
50.0
Capacity Margin MBper Second
13.636363636363633
Stock Control Duty At Minimum Demand
0.7272727272727273
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
Required Wood Vinegar MBper Second
727.2727272727273
Other Fraction Credit MBper Second
Aceticacid
72.72727272727273
Methanol
218.1818181818182
Bioethanol
7.2727272727272725
Credit Use
Direct36.364acetone plus36.364from its72.727acetic acid covers72.727raw-gasoline acetone.218.182methanol exceeds72.727demand. Remaining fractions are separately stored.
PF017

Acetone from wood-vinegar acetic acid

Include; proposed producer capacity
Acetone from wood-vinegar acetic acid
Offline wiki reference / native texture

Proposed quantity

1

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
1,169
Recipe
Map
gt.recipe.largechemicalreactor
Ordinal
759
M EUt
480
M Duration
400
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
  • Calcium Dust × 0 gregtech:gt.metaitem.01 @2026
  • Programmed Circuit × 0 gregtech:gt.integrated_circuit @3
Outputs
None recorded
Fluid Inputs
  • Name
    aceticacid
    Amount
    2,000
Fluid Outputs
  • Name
    acetone
    Amount
    1,000
  • Name
    carbondioxide
    Amount
    1,000
  • Name
    water
    Amount
    1,000
Metadata
Voltage
512
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
480
Max Electrical Draw Bank EUt
480
Actual Duration Ticks
400
Selected Fluid
acetone
Selected Fluid Minimum Demand MBper Second
36.36363636363637
Native Electrical Capacity MBper Second
50.0
Capacity Margin MBper Second
13.636363636363633
Stock Control Duty At Minimum Demand
0.7272727272727273
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
Reusable Catalyst
Native zero-amount Calcium Dust; keep a dedicated non-consumed catalyst slot.
PF018

Renewable air/nitrogen separation

Include; proposed producer capacity
Renewable air/nitrogen separation
Offline wiki reference / native texture
More reference pictures
Renewable air/nitrogen separation
Offline wiki reference / native texture

Proposed quantity

1

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
790
Recipe
Map
gtpp.recipe.multicentrifuge
Ordinal
22
M EUt
8
M Duration
1,600
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
None recorded
Outputs
None recorded
Fluid Inputs
  • Name
    air
    Amount
    10,000
Fluid Outputs
  • Name
    oxygen
    Amount
    1,000
  • Name
    nitrogen
    Amount
    3,900
Metadata
Voltage
128
Working Amps
4
Parallel Recipes
12
Max Electrical Draw Per Machine EUt
346
Max Electrical Draw Bank EUt
346
Actual Duration Ticks
355
Selected Fluid
nitrogen
Selected Fluid Minimum Demand MBper Second
1,869.090909090909
Native Electrical Capacity MBper Second
2,636.6197183098593
Capacity Margin MBper Second
767.5288092189503
Stock Control Duty At Minimum Demand
0.7088966588966589
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
Intake Metadata
861
Intake Quantity
1
Intake Capacity Air MBper Second
5,000
Required Air MBper Second
4,792.540792540793
Maximum Nitrogen With Actual Intake MBper Second
1,950.0
Oxygen Byproduct At Demand MBper Second
479.2540792540792
Native Modifiers
EU
0.8999999761581421
Duration
0.4444444477558136
Air Flow Caveat
The electrical maximum needs 6,760.563 air/s; one intake supplies 5,000. Selected 1,869.091 nitrogen/s including both wood-pyro branches needs 4,792.541 air/s and fits the real intake. Its front must remain open.
PF019

Water electrolysis for hydrogen and oxygen

Include; proposed producer capacity
Water electrolysis for hydrogen and oxygen
Offline wiki reference / native texture

Proposed quantity

3

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
796
Recipe
Map
gtpp.recipe.multielectro
Ordinal
91
M EUt
30
M Duration
2,000
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
  • Programmed Circuit × 0 gregtech:gt.integrated_circuit @1
Outputs
None recorded
Fluid Inputs
  • Name
    water
    Amount
    1,000
Fluid Outputs
  • Name
    oxygen
    Amount
    1,000
  • Name
    hydrogen
    Amount
    2,000
Metadata
Voltage
2,048
Working Amps
4
Parallel Recipes
8
Max Electrical Draw Per Machine EUt
3,456
Max Electrical Draw Bank EUt
10,368
Actual Duration Ticks
178
Selected Fluid
hydrogen
Selected Fluid Minimum Demand MBper Second
3,500
Native Electrical Capacity MBper Second
5,393.258426966292
Capacity Margin MBper Second
1,893.258426966292
Stock Control Duty At Minimum Demand
0.6489583333333333
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
Oxygen Bank Capacity MBper Second
2,696.629213483146
Water Bank Maximum MBper Second
2,696.629213483146
Native Modifiers
EU
0.8999999761581421
Duration
0.3571428656578064
Demand Lower Bound Details
Hydrocracking2560H2/s; light1250/6=208.333; fullnaphtha3750/6=625; gas145.455/8=18.182; heavy38.636/4=9.659; total3421.174H2/s before independent utilities.3500selected target includes a small margin; any extra factory consumers receive separate sizing.
PF020

Oxygen liquefaction

Include; proposed producer capacity
Oxygen liquefaction
Offline wiki reference / native texture

Proposed quantity

5

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
910
Recipe
Map
gtpp.recipe.cryogenicfreezer
Ordinal
150
M EUt
480
M Duration
1,200
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
None recorded
Outputs
None recorded
Fluid Inputs
  • Name
    oxygen
    Amount
    1,000
Fluid Outputs
  • Name
    liquidoxygen
    Amount
    1,000
Metadata
Voltage
512
Working Amps
4
Parallel Recipes
4
Max Electrical Draw Per Machine EUt
1,728
Max Electrical Draw Bank EUt
8,640
Actual Duration Ticks
545
Selected Fluid
liquidoxygen
Selected Fluid Minimum Demand MBper Second
640
Native Electrical Capacity MBper Second
733.9449541284404
Capacity Margin MBper Second
93.94495412844037
Stock Control Duty At Minimum Demand
0.872
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
Native Modifiers
EU
0.8999999761581421
Duration
0.45454543828964233
Cryotheum MBper Second Bank
50
Exact Detached Calculation Receipt
result-review-final-feed-and-casting-20261012.json
Oxygen Source
PF019 already supplies at least1750O2/s at the selected3500H2/s operation; PF004 needs480O2/s and PF020640O2/s. Nitrogen branch oxygen is additional stored supply.
PF021

Cryotheum fluid extraction

Include; proposed producer capacity
Cryotheum fluid extraction
Offline wiki reference / native texture

Proposed quantity

3

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
513
Recipe
Map
gt.recipe.fluidextractor
Ordinal
114
M EUt
240
M Duration
200
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
  • Cryotheum Dust × 1 gregtech:gt.metaitem.01 @2898
Outputs
None recorded
Fluid Inputs
None recorded
Fluid Outputs
  • Name
    cryotheum
    Amount
    250
Metadata
Voltage
512
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
240
Max Electrical Draw Bank EUt
720
Actual Duration Ticks
200
Selected Fluid
cryotheum
Selected Fluid Minimum Demand MBper Second
50
Native Electrical Capacity MBper Second
75.0
Capacity Margin MBper Second
25.0
Stock Control Duty At Minimum Demand
0.6666666666666666
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
Required Dust Per Second
0.2
Dust Key
gregtech:gt.metaitem.01@2898
PF022

Lubricant brewing

Include; proposed producer capacity
Lubricant brewing
Offline wiki reference / native texture

Proposed quantity

2

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
491
Recipe
Map
gt.recipe.brewer
Ordinal
325
M EUt
4
M Duration
128
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
  • Talc × 1 gregtech:gt.metaitem.01 @2902
Outputs
None recorded
Fluid Inputs
  • Name
    creosote
    Amount
    750
Fluid Outputs
  • Name
    lubricant
    Amount
    750
Metadata
Voltage
32
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
4
Max Electrical Draw Bank EUt
8
Actual Duration Ticks
128
Selected Fluid
lubricant
Selected Fluid Minimum Demand MBper Second
35.55555555555556
Native Electrical Capacity MBper Second
234.375
Capacity Margin MBper Second
198.81944444444446
Stock Control Duty At Minimum Demand
0.1517037037037037
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
Required Creosote MBper Second
35.55555555555556
Required Talc Per Second
0.04740740740740741
Native Electrical Calculation
Detached calculator confirms4EU/t128ticks; do not invent an LV16EU/t overclock.
PF023

Heavy-fuel desulfurization

Include; proposed producer capacity
Heavy-fuel desulfurization
Offline wiki reference / native texture

Proposed quantity

1

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
1,169
Recipe
Map
gt.recipe.largechemicalreactor
Ordinal
867
M EUt
30
M Duration
160
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
  • Programmed Circuit × 0 gregtech:gt.integrated_circuit @4
Outputs
None recorded
Fluid Inputs
  • Name
    liquid_sulfuricheavy_fuel
    Amount
    8,000
  • Name
    hydrogen
    Amount
    2,000
Fluid Outputs
  • Name
    liquid_heavy_fuel
    Amount
    8,000
  • Name
    liquid_hydricsulfur
    Amount
    1,000
Metadata
Recipe Metadata Key{clazz=java.lang.Boolean, identifier=cleanroom'}
false
Voltage
32
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
30
Max Electrical Draw Bank EUt
30
Actual Duration Ticks
160
Selected Fluid
liquid_heavy_fuel
Selected Fluid Minimum Demand MBper Second
38.636363636363626
Native Electrical Capacity MBper Second
1,000.0
Capacity Margin MBper Second
961.3636363636364
Stock Control Duty At Minimum Demand
0.03863636363636363
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
PF024

Wood-vinegar pyrolysis

Include; proposed producer capacity
Wood-vinegar pyrolysis
Offline wiki reference / native texture
More reference pictures
Wood-vinegar pyrolysis
Offline wiki reference / native texture

Proposed quantity

2

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
1,159
Recipe
Map
gt.recipe.pyro
Ordinal
144
M EUt
96
M Duration
320
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
  • Oak Log × 16 minecraft:log @32767
  • Programmed Circuit × 0 gregtech:gt.integrated_circuit @8
Outputs
  • Charcoal × 20 minecraft:coal @1
Fluid Inputs
  • Name
    nitrogen
    Amount
    1,000
Fluid Outputs
  • Name
    woodvinegar
    Amount
    3,000
Metadata
Voltage
512
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
384
Max Electrical Draw Bank EUt
768
Actual Duration Ticks
160
Selected Fluid
woodvinegar
Selected Fluid Minimum Demand MBper Second
727.2727272727273
Native Electrical Capacity MBper Second
750.0
Capacity Margin MBper Second
22.727272727272748
Stock Control Duty At Minimum Demand
0.9696969696969697
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
Coil
Kanthal tier1: native duration modifier2/(1+1)=1; ordinary HV OC96→384EU/t,320→160ticks.
Log Minimum Per Second
3.878787878787879
Nitrogen Minimum MBPer Second
242.4242424242424
Charcoal At Demand Per Second
4.848484848484848
Tree Feed
Reserve measured >=4.1logs/s from the automated tree sector for wood vinegar plus creosote. Root saplings/tool replacement and AE buffer limits remain part of the renewable feed.
PF025

Creosote/charcoal pyrolysis

Include; proposed producer capacity
Creosote/charcoal pyrolysis
Offline wiki reference / native texture
More reference pictures
Creosote/charcoal pyrolysis
Offline wiki reference / native texture

Proposed quantity

1

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
1,159
Recipe
Map
gt.recipe.pyro
Ordinal
137
M EUt
64
M Duration
640
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
  • Oak Log × 16 minecraft:log @32767
  • Programmed Circuit × 0 gregtech:gt.integrated_circuit @1
Outputs
  • Charcoal × 20 minecraft:coal @1
Fluid Inputs
None recorded
Fluid Outputs
  • Name
    creosote
    Amount
    4,000
Metadata
Voltage
128
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
64
Max Electrical Draw Bank EUt
64
Actual Duration Ticks
640
Selected Fluid
creosote
Selected Fluid Minimum Demand MBper Second
35.55555555555556
Native Electrical Capacity MBper Second
125.0
Capacity Margin MBper Second
89.44444444444444
Stock Control Duty At Minimum Demand
0.28444444444444444
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
Coil
Kanthal tier1 duration modifier1; single MV hatch128 does not overclock the64EU/t recipe.
Log Minimum Per Second
0.14222222222222222
Charcoal At Demand Per Second
0.17777777777777778
PF026

Cryotheum dust mixing

Include; proposed producer capacity
Cryotheum dust mixing
Offline wiki reference / native texture

Proposed quantity

2

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
582
Recipe
Map
gt.recipe.mixer
Ordinal
219
M EUt
120
M Duration
160
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
  • Saltpeter Dust × 1 gregtech:gt.metaitem.01 @2836
  • Snow Powder × 1 gregtech:gt.metaitem.01 @2728
  • Redstone Dust × 1 minecraft:redstone @0
  • Blizz Dust × 1 gregtech:gt.metaitem.01 @2851
Outputs
  • Cryotheum Dust × 1 gregtech:gt.metaitem.01 @2898
Fluid Inputs
None recorded
Fluid Outputs
None recorded
Metadata
Voltage
128
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
120
Max Electrical Draw Bank EUt
240
Actual Duration Ticks
160
Selected Item Damage
2,898
Required Items Per Second
0.2
Native Electrical Capacity Items Per Second
0.25
Picture Caption
Installed machine-family reference; dedicated proposed production recipe is attached.
PF027

Snow powder maceration

Include; proposed producer capacity
Snow powder maceration
Offline wiki reference / native texture

Proposed quantity

1

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
301
Recipe
Map
gt.recipe.macerator
Ordinal
8,908
M EUt
4
M Duration
16
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
  • Snowball × 1 minecraft:snowball @32767
Outputs
  • Snow Powder × 1 gregtech:gt.metaitem.01 @2728
Fluid Inputs
None recorded
Fluid Outputs
None recorded
Metadata
Voltage
32
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
4
Max Electrical Draw Bank EUt
4
Actual Duration Ticks
16
Selected Item Damage
2,728
Required Items Per Second
0.2
Native Electrical Capacity Items Per Second
1.25
Picture Caption
Installed machine-family reference; dedicated proposed production recipe is attached.
PF028

Renewable benzene-feed wood-tar pyrolysis

Include; proposed producer capacity
Renewable benzene-feed wood-tar pyrolysis
Offline wiki reference / native texture
More reference pictures
Renewable benzene-feed wood-tar pyrolysis
Offline wiki reference / native texture

Proposed quantity

6

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
1,159
Recipe
Map
gt.recipe.pyro
Ordinal
146
M EUt
96
M Duration
320
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
  • Oak Log × 16 minecraft:log @32767
  • Programmed Circuit × 0 gregtech:gt.integrated_circuit @10
Outputs
  • Charcoal × 20 minecraft:coal @1
Fluid Inputs
  • Name
    nitrogen
    Amount
    1,000
Fluid Outputs
  • Name
    woodtar
    Amount
    1,500
Metadata
Voltage
512
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
384
Max Electrical Draw Bank EUt
2,304
Actual Duration Ticks
160
Selected Fluid
woodtar
Selected Fluid Minimum Demand MBper Second
1,000
Native Electrical Capacity MBper Second
1,125.0
Capacity Margin MBper Second
125.0
Stock Control Duty At Minimum Demand
0.8888888888888888
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
Coil
Kanthal tier1, one ordinary HV OC;96→384EU/t and320→160ticks.
Nitrogen Minimum MBPer Second
666.6666666666666
Logs Minimum Per Second
10.666666666666666
Charcoal At Demand Per Second
13.333333333333334
Quantity Correction
Six ovens, not five:1500tar per160ticks gives187.5mB/s each; six supply1125tar/s, enough to sustain1000tar/s into two towers.
PF029

Additional renewable benzene distillation

Include; proposed producer capacity
Additional renewable benzene distillation
Offline wiki reference / native texture
More reference pictures
Additional renewable benzene distillation
Offline wiki reference / native texture
Additional renewable benzene distillation
Offline wiki reference / native texture

Proposed quantity

2

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
1,126
Recipe
Map
gt.recipe.distillationtower
Ordinal
58
M EUt
256
M Duration
40
M Special Value
0
M Enabled
Yes
M Fake Recipe
No
M Hidden
No
Is NBTSensitive
No
Inputs
  • Programmed Circuit × 0 gregtech:gt.integrated_circuit @2
Outputs
None recorded
Fluid Inputs
  • Name
    woodtar
    Amount
    1,000
Fluid Outputs
  • Name
    creosote
    Amount
    250
  • Name
    phenol
    Amount
    100
  • Name
    benzene
    Amount
    400
  • Name
    liquid_toluene
    Amount
    100
  • Name
    1,3dimethylbenzene
    Amount
    150
Metadata
Voltage
512
Working Amps
1
Parallel Recipes
1
Max Electrical Draw Per Machine EUt
256
Max Electrical Draw Bank EUt
512
Actual Duration Ticks
40
Selected Fluid
benzene
Selected Fluid Minimum Demand MBper Second
400
Native Electrical Capacity MBper Second
400.0
Capacity Margin MBper Second
0.0
Stock Control Duty At Minimum Demand
1.0
Owner Semantics
Native perfect4/4OC for LCR; otherwise ordinary4EU/2timeOC unless explicit GT++ modifiers attached. Single normal hatch uses1workingA; two ordinary hatches2Aeach use4total.
Acceptance
Calculated current recipe/owner capability; actual hatch formation, throughput and tank recovery will be tested during authorized implementation, not claimed as present machinery.
Picture Caption
Reference for the named installed machine family; the exact producer count, material grade and source recipes are the editable proposal, not a photograph of an existing factory.
Woodtar Required MBPer Second
1,000
Purpose
Supplies the remote oil rigs independently of their own oil until the staged refinery also supplies450benzene/s. Retain creosote, phenol, toluene and xylene byproducts; no infinite oil loop.
PF-AUX-oilOutposts

Fluid Drilling Rig III

Include; proposed producer capacity
Fluid Drilling Rig III
Offline wiki reference / native texture
More reference pictures
Fluid Drilling Rig III
Offline wiki reference / native texture
Fluid Drilling Rig III
Offline wiki reference / native texture

Proposed quantity

4

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.

Power And Supply

Local Generator Metadata
1,118
Name
Turbo Gas Turbine II
Quantity
4
Native Output Voltage
2,048
Native Output Amperage
1
Native Efficiency Percent
60
Raw Fuel EUper MB
360
Actual Benzene EUPer MB
216
Local Assembly Per Rig
One EV1118 generator front output through a short EV-rated cable into that rig EV44 energy hatch; native164352EU generator buffer smooths1mB fuel operations. One filtered Ender Tank receiver plus a64,000mB local benzene buffer per rig. Matched shared-color central send tank carries the same canonical fluid. AE wireless is not a cross-dimensional EU link.
Electrical Demand EUt Per Rig
1,792
Native Fuel MBper Second Four Rigs At Demand
663.7037037037037
Native Fuel MBper Second Four At Full EVOutput
758.5185185185185
Conservative Integer Provision MBper Second
800
Credited Refinery Benzene MBper Second
450
Additional Renewable Benzene MBper Second
400
Total Benzene Supply MBper Second
850
Margin At Rig Demand MBper Second
186.2962962962963
Margin At Full EVOutput MBper Second
91.48148148148152
Margin At Conservative Integer Provision MBper Second
50
Existing Source Receipt
native-remote-benzene-current.json
Central Power Accounting
The actual remote7,168EU/t is generated on site from budgeted benzene. Central source production is already in the producerBOM; retain7,168EU/t equivalent headroom inside65,536service reserve conservatively, but do not claim it is additional central cable load.
Startup
Precharge the reviewed ordinary energy reserve using eligible lower-tier generation, or the proposed EV solar array after actual sky/day/weather checks. Start renewable wood-tar benzene first, then two rigs (331.852benzene/s), third after refinery byproduct increases, then fourth. Only add the full factory/room endpoints after sustainable fuel buffers recover. The finite initial fuel/energy buffers are startup stock, not endless generation.
Full native requirements and source evidence
Controller Metadata
142
Energy Voltage
2,048
EUt Each
1,792
EUt Bank
7,168
Native Formula
-(7 << (2*voltageTier)), EVtier4 gives1792EU/t;4×4chunk range,8tick pumping cycle.
Minimum Output MBper Operation Each
250
Required Total Medium Oil MBper Second
2,500
First Source Boundary
Only surveyed existing medium-oil fields satisfying this actual sustained flow are selected. Four is a starting quantity, not a promise every random field yields enough; relocate/add admissible outposts or reduce enabled engine count when field output falls. No oil reserve is infinite. Remote pump power is included in the replenishment reserve.
PF-AUX-steamUtility

Large Bronze Boiler

Include; proposed producer capacity
Large Bronze Boiler
Offline wiki reference / native texture
More reference pictures
Large Bronze Boiler
Offline wiki reference / native texture
Large Bronze Boiler
Offline wiki reference / native texture

Proposed quantity

1

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Controller Metadata
1,020
Native Steam Capacity MBper Second
16,000
Required Steam MBper Second
2,980
Coal Equivalent Per Second At Demand
0.093125
Normal Steam Water Minimum MBper Second
18.625
EU/t
0
Fuel Source
Renewable tree charcoal; ordinary steam recipes use steam, not superheatedsteam. Independent water and fuel buffers plus low-water shutdown are required.
PF-AUX-farmSectorProtectedInputs

Farm Sector Protected Inputs

Include; proposed producer capacity

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Budget Owner
The separate 24,576 EU/t protected farm sector; do not count the same farm power twice as new fuel-factory production.
Cold Blaze
Native Mob Row
M057
Species
Evolved Cold Blaze
First Capture Dimension
Europa, rocket tier3
Controller
14,201
Proposed Dedicated EEC
1
Ordinary Drop
GT Blizz Dust2851,50% ordinary chance, no player-only or conditional modifier
Minimum Blizz Dust Items Per Second
0.2
Minimum Expected Kills Per Second
0.4
Snowman
Native Mob Row
M104
Species
Vanilla Snowman
Controller
14,201
Proposed Dedicated EEC
1
Ordinary Drop
minecraft:snowball@0 amount8, no player-only or special condition; native SoulVial accepts it
Minimum Snowballs Per Second
0.2
Minimum Expected Kills Per Second
0.025
Reservation Rule
Reserve fuel-stock recovery first within the farm sector, using actual captured mob PoweredSpawners and native EEC processing. Measure output under the selected legal operating voltage; do not claim chance-based drops are guaranteed per kill. Other farm jobs queue behind this replenishment when buffer thresholds are low.
First Resource Witness
runtime-mob-drops.json
Concurrency
All30mob cells and13activecrop managers share scheduling within24,576EU/t. ColdBlaze/Snowman fuel-stock replenishment has priority; no claim that30IV EECs operate simultaneously. Remaining farm jobs queue and use duty cycling.
PF-AUX-renewableTreeFeed

Renewable Tree Feed

Include; proposed producer capacity

Automation

Stock-controlled native process; retain catalysts and circuit settings, supply inputs continuously, import usable outputs and byproducts into AE2. Shut down on missing feed, unsafe fluid levels or full buffers.

AE2 Storage

Dedicated fluid partition and visible working tank; exact recipe outputs and feed rates are retained below.
Full native requirements and source evidence
Minimum Logs Per Second
14.687676767676766
Planned Reservation Logs Per Second
15.5
Source
Existing proposed automated ordinary-oak tree/TGS production; reserve this common renewable feed ahead of decorative species or surplus burns. Actual sustained harvest/tool/fertilizer recovery is an implementation acceptance check.
Charcoal Credit Items Per Second
18.35959595959596
Boiler Coal Equivalent Needed Per Second
0.093125