<?xml version="1.0"?>
<feed xmlns="http://www.w3.org/2005/Atom" xml:lang="en">
	<id>https://wiki.opensourceecology.org/index.php?action=history&amp;feed=atom&amp;title=Nickel_Iron_Battery_Manufacturing</id>
	<title>Nickel Iron Battery Manufacturing - Revision history</title>
	<link rel="self" type="application/atom+xml" href="https://wiki.opensourceecology.org/index.php?action=history&amp;feed=atom&amp;title=Nickel_Iron_Battery_Manufacturing"/>
	<link rel="alternate" type="text/html" href="https://wiki.opensourceecology.org/index.php?title=Nickel_Iron_Battery_Manufacturing&amp;action=history"/>
	<updated>2026-05-02T09:28:43Z</updated>
	<subtitle>Revision history for this page on the wiki</subtitle>
	<generator>MediaWiki 1.39.13</generator>
	<entry>
		<id>https://wiki.opensourceecology.org/index.php?title=Nickel_Iron_Battery_Manufacturing&amp;diff=321506&amp;oldid=prev</id>
		<title>Marcin: /* Main Readout */</title>
		<link rel="alternate" type="text/html" href="https://wiki.opensourceecology.org/index.php?title=Nickel_Iron_Battery_Manufacturing&amp;diff=321506&amp;oldid=prev"/>
		<updated>2026-03-16T01:19:04Z</updated>

		<summary type="html">&lt;p&gt;&lt;span dir=&quot;auto&quot;&gt;&lt;span class=&quot;autocomment&quot;&gt;Main Readout&lt;/span&gt;&lt;/span&gt;&lt;/p&gt;
&lt;a href=&quot;https://wiki.opensourceecology.org/index.php?title=Nickel_Iron_Battery_Manufacturing&amp;amp;diff=321506&amp;amp;oldid=321505&quot;&gt;Show changes&lt;/a&gt;</summary>
		<author><name>Marcin</name></author>
	</entry>
	<entry>
		<id>https://wiki.opensourceecology.org/index.php?title=Nickel_Iron_Battery_Manufacturing&amp;diff=321505&amp;oldid=prev</id>
		<title>Marcin: Created page with &quot;= NiFe Factory Material and Plate Model for 20 MWh/year =  Assumptions: * Plant output: 20,000 kWh/year * Planning mass intensity: 20 kg/kWh finished wet battery * Total finished battery mass: 400 t/year * 20-foot container payload basis: 28.3 t/container * Plate area model: 40 mg/cm² coated-face loading, 75% utilization, 1.2 V nominal * Resulting areal energy density used for sizing: 104 Wh/m² of coated face  {| class=&quot;wikitable sortable&quot; ! Material / Metric ! Unit ba...&quot;</title>
		<link rel="alternate" type="text/html" href="https://wiki.opensourceecology.org/index.php?title=Nickel_Iron_Battery_Manufacturing&amp;diff=321505&amp;oldid=prev"/>
		<updated>2026-03-16T00:49:16Z</updated>

		<summary type="html">&lt;p&gt;Created page with &amp;quot;= NiFe Factory Material and Plate Model for 20 MWh/year =  Assumptions: * Plant output: 20,000 kWh/year * Planning mass intensity: 20 kg/kWh finished wet battery * Total finished battery mass: 400 t/year * 20-foot container payload basis: 28.3 t/container * Plate area model: 40 mg/cm² coated-face loading, 75% utilization, 1.2 V nominal * Resulting areal energy density used for sizing: 104 Wh/m² of coated face  {| class=&amp;quot;wikitable sortable&amp;quot; ! Material / Metric ! Unit ba...&amp;quot;&lt;/p&gt;
&lt;p&gt;&lt;b&gt;New page&lt;/b&gt;&lt;/p&gt;&lt;div&gt;= NiFe Factory Material and Plate Model for 20 MWh/year =&lt;br /&gt;
&lt;br /&gt;
Assumptions:&lt;br /&gt;
* Plant output: 20,000 kWh/year&lt;br /&gt;
* Planning mass intensity: 20 kg/kWh finished wet battery&lt;br /&gt;
* Total finished battery mass: 400 t/year&lt;br /&gt;
* 20-foot container payload basis: 28.3 t/container&lt;br /&gt;
* Plate area model: 40 mg/cm² coated-face loading, 75% utilization, 1.2 V nominal&lt;br /&gt;
* Resulting areal energy density used for sizing: 104 Wh/m² of coated face&lt;br /&gt;
&lt;br /&gt;
{| class=&amp;quot;wikitable sortable&amp;quot;&lt;br /&gt;
! Material / Metric&lt;br /&gt;
! Unit basis&lt;br /&gt;
! Per kWh&lt;br /&gt;
! Annual total for 20 MWh&lt;br /&gt;
! Commodity cost&lt;br /&gt;
! Commodity $/kWh&lt;br /&gt;
! Annual commodity cost&lt;br /&gt;
! Integrated $/kWh&lt;br /&gt;
! Annual integrated cost&lt;br /&gt;
! 20 ft containers by weight&lt;br /&gt;
|-&lt;br /&gt;
| Nickel, contained metal&lt;br /&gt;
| kg&lt;br /&gt;
| 1.20&lt;br /&gt;
| 24.0 t&lt;br /&gt;
| $17.34/kg&lt;br /&gt;
| $20.81&lt;br /&gt;
| $416,160&lt;br /&gt;
| $20.81&lt;br /&gt;
| $416,160&lt;br /&gt;
| 0.85&lt;br /&gt;
|-&lt;br /&gt;
| Nickel hydroxide equivalent&lt;br /&gt;
| kg&lt;br /&gt;
| 1.90&lt;br /&gt;
| 37.9 t&lt;br /&gt;
| derived from nickel content&lt;br /&gt;
| n/a&lt;br /&gt;
| n/a&lt;br /&gt;
| n/a&lt;br /&gt;
| n/a&lt;br /&gt;
| 1.34&lt;br /&gt;
|-&lt;br /&gt;
| Iron powder&lt;br /&gt;
| kg&lt;br /&gt;
| 5.50&lt;br /&gt;
| 110.0 t&lt;br /&gt;
| $2.00/kg purchased&lt;br /&gt;
| $11.00&lt;br /&gt;
| $220,000&lt;br /&gt;
| $4.40&lt;br /&gt;
| $88,000&lt;br /&gt;
| 3.89&lt;br /&gt;
|-&lt;br /&gt;
| Steel mesh / sheet / case internals&lt;br /&gt;
| kg&lt;br /&gt;
| 6.00&lt;br /&gt;
| 120.0 t&lt;br /&gt;
| $1.018/kg purchased&lt;br /&gt;
| $6.11&lt;br /&gt;
| $122,160&lt;br /&gt;
| $3.60&lt;br /&gt;
| $72,000&lt;br /&gt;
| 4.24&lt;br /&gt;
|-&lt;br /&gt;
| KOH, dry basis&lt;br /&gt;
| kg&lt;br /&gt;
| 2.00&lt;br /&gt;
| 40.0 t&lt;br /&gt;
| $0.91/kg&lt;br /&gt;
| $1.82&lt;br /&gt;
| $36,400&lt;br /&gt;
| $1.82&lt;br /&gt;
| $36,400&lt;br /&gt;
| 1.41&lt;br /&gt;
|-&lt;br /&gt;
| HDPE / PP case resin&lt;br /&gt;
| kg&lt;br /&gt;
| 1.00&lt;br /&gt;
| 20.0 t&lt;br /&gt;
| $0.87/kg&lt;br /&gt;
| $0.87&lt;br /&gt;
| $17,400&lt;br /&gt;
| $0.87&lt;br /&gt;
| $17,400&lt;br /&gt;
| 0.71&lt;br /&gt;
|-&lt;br /&gt;
| Copper bus bars / terminals&lt;br /&gt;
| kg&lt;br /&gt;
| 0.30&lt;br /&gt;
| 6.0 t&lt;br /&gt;
| $12.758/kg&lt;br /&gt;
| $3.83&lt;br /&gt;
| $76,548&lt;br /&gt;
| $3.83&lt;br /&gt;
| $76,548&lt;br /&gt;
| 0.21&lt;br /&gt;
|-&lt;br /&gt;
| Separator + binder + additives&lt;br /&gt;
| kg&lt;br /&gt;
| 0.80&lt;br /&gt;
| 16.0 t&lt;br /&gt;
| $3.00/kg assumed&lt;br /&gt;
| $2.40&lt;br /&gt;
| $48,000&lt;br /&gt;
| $2.40&lt;br /&gt;
| $48,000&lt;br /&gt;
| 0.57&lt;br /&gt;
|-&lt;br /&gt;
| Deionized water&lt;br /&gt;
| kg&lt;br /&gt;
| 3.20&lt;br /&gt;
| 64.0 t&lt;br /&gt;
| $0.001/kg assumed&lt;br /&gt;
| $0.00&lt;br /&gt;
| $64&lt;br /&gt;
| $0.00&lt;br /&gt;
| $64&lt;br /&gt;
| 2.26&lt;br /&gt;
|-&lt;br /&gt;
! Total&lt;br /&gt;
! &lt;br /&gt;
! 20.00 kg&lt;br /&gt;
! 400.0 t&lt;br /&gt;
! &lt;br /&gt;
! $46.84/kWh&lt;br /&gt;
! $936,732&lt;br /&gt;
! $37.73/kWh&lt;br /&gt;
! $754,572&lt;br /&gt;
! 14.13&lt;br /&gt;
|}&lt;br /&gt;
&lt;br /&gt;
= Electrode Plate Area Model =&lt;br /&gt;
&lt;br /&gt;
The next table is for factory sizing of the electrode fabrication line.&lt;br /&gt;
It uses the aggressive planning assumption of 104 Wh/m² of coated face.&lt;br /&gt;
&lt;br /&gt;
{| class=&amp;quot;wikitable&amp;quot;&lt;br /&gt;
! Plate metric&lt;br /&gt;
! Formula basis&lt;br /&gt;
! Per kWh&lt;br /&gt;
! Annual total for 20 MWh&lt;br /&gt;
|-&lt;br /&gt;
| Positive coated-face area&lt;br /&gt;
| 1000 Wh / 104 Wh/m²&lt;br /&gt;
| 9.62 m²&lt;br /&gt;
| 192,308 m²&lt;br /&gt;
|-&lt;br /&gt;
| Negative coated-face area&lt;br /&gt;
| matched to positive area&lt;br /&gt;
| 9.62 m²&lt;br /&gt;
| 192,308 m²&lt;br /&gt;
|-&lt;br /&gt;
| Total coated-face area, both polarities&lt;br /&gt;
| positive + negative&lt;br /&gt;
| 19.23 m²&lt;br /&gt;
| 384,615 m²&lt;br /&gt;
|-&lt;br /&gt;
| Positive metal-sheet plate area&lt;br /&gt;
| double-coated plates, so coated-face area / 2&lt;br /&gt;
| 4.81 m²&lt;br /&gt;
| 96,154 m²&lt;br /&gt;
|-&lt;br /&gt;
| Negative metal-sheet plate area&lt;br /&gt;
| double-coated plates, so coated-face area / 2&lt;br /&gt;
| 4.81 m²&lt;br /&gt;
| 96,154 m²&lt;br /&gt;
|-&lt;br /&gt;
| Total metal-sheet electrode area&lt;br /&gt;
| positive sheet + negative sheet&lt;br /&gt;
| 9.62 m²&lt;br /&gt;
| 192,308 m²&lt;br /&gt;
|}&lt;br /&gt;
&lt;br /&gt;
= Shipping Container Summary =&lt;br /&gt;
&lt;br /&gt;
{| class=&amp;quot;wikitable&amp;quot;&lt;br /&gt;
! Shipping item&lt;br /&gt;
! Annual tonnage&lt;br /&gt;
! 20 ft containers at 28.3 t payload&lt;br /&gt;
|-&lt;br /&gt;
| Finished wet batteries&lt;br /&gt;
| 400.0 t&lt;br /&gt;
| 14.13&lt;br /&gt;
|-&lt;br /&gt;
| All nickel input, contained metal basis&lt;br /&gt;
| 24.0 t&lt;br /&gt;
| 0.85&lt;br /&gt;
|-&lt;br /&gt;
| Iron powder&lt;br /&gt;
| 110.0 t&lt;br /&gt;
| 3.89&lt;br /&gt;
|-&lt;br /&gt;
| Steel&lt;br /&gt;
| 120.0 t&lt;br /&gt;
| 4.24&lt;br /&gt;
|-&lt;br /&gt;
| KOH&lt;br /&gt;
| 40.0 t&lt;br /&gt;
| 1.41&lt;br /&gt;
|-&lt;br /&gt;
| Everything except water&lt;br /&gt;
| 336.0 t&lt;br /&gt;
| 11.87&lt;br /&gt;
|}&lt;br /&gt;
&lt;br /&gt;
= Main Readout =&lt;br /&gt;
&lt;br /&gt;
* A 20 MWh/year NiFe plant at 20 kg/kWh is about 400 t/year of finished battery output.&lt;br /&gt;
* On purchased materials, this planning model lands near $46.84/kWh.&lt;br /&gt;
* With aggressive in-house iron and steel integration, the same model lands near $37.73/kWh.&lt;br /&gt;
* Finished-battery outbound logistics are about 14 standard 20-foot containers per year by weight.&lt;br /&gt;
* The electrode line must process about 384,615 m²/year of coated electrode faces under the plate-loading assumption used here.&lt;/div&gt;</summary>
		<author><name>Marcin</name></author>
	</entry>
</feed>