JP7831391B2 - Manufacturing method for fuel cell separators - Google Patents
Manufacturing method for fuel cell separatorsInfo
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- JP7831391B2 JP7831391B2 JP2023078737A JP2023078737A JP7831391B2 JP 7831391 B2 JP7831391 B2 JP 7831391B2 JP 2023078737 A JP2023078737 A JP 2023078737A JP 2023078737 A JP2023078737 A JP 2023078737A JP 7831391 B2 JP7831391 B2 JP 7831391B2
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
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Description
本発明は燃料電池用セパレータの製造方法に関する。 This invention relates to a method for manufacturing a separator for fuel cells.
電解質膜を用いた固体高分子型燃料電池(以下、燃料電池と記載する)は、低温における作動が可能であり、且つ小型軽量化が可能であるため、自動車等への適用が検討されている。 Solid polymer fuel cells (hereinafter referred to as "fuel cells"), which use electrolyte membranes, can operate at low temperatures and can be made smaller and lighter, making them suitable for use in automobiles and other applications.
このような燃料電池では、基本単位であるセル(単電池)が複数積層されている。セルは、一対のガス拡散層(Gas Diffusion Layer:GDL)が両側に配置された膜電極接合体と、これらを挟持している一対のセパレータとを備えている。膜電極接合体は、イオン交換膜である電解質膜の両側にアノード側の電極及びカソード側の電極を配置した構造を有している。 In such fuel cells, multiple cells (single cells), which are the basic units, are stacked. Each cell comprises a membrane electrode assembly with a pair of gas diffusion layers (GDLs) on both sides, and a pair of separators sandwiching these. The membrane electrode assembly has a structure in which an anode electrode and a cathode electrode are positioned on both sides of an electrolyte membrane, which is an ion-exchange membrane.
燃料電池用セパレータとしては、耐食性に優れ、安価なステンレス製のセパレータが広く用いられている。ステンレス製セパレータは、一般にクロム酸化物(一般にCr2O3)の不働態被膜によって耐食性を確保しているが、詳細な不働態被膜成分としてはFeOやFeOHのような酸化物や水酸化物が実際には存在する。また、燃料電池の運転の際に用いられる冷却水や、運転中に生成する生成水等の液水にステンレス表面が晒されていると、ステンレスが腐食してしまう場合がある。このため、燃料電池用セパレータにステンレス基材を用いる場合には、耐食性のさらなる向上が必要となる部位が存在する。 Stainless steel separators, which offer excellent corrosion resistance and are inexpensive, are widely used as separators for fuel cells. While stainless steel separators generally achieve corrosion resistance through a passive film of chromium oxide (typically Cr₂O₃ ), the actual components of this passive film include oxides and hydroxides such as FeO and FeOH. Furthermore, exposure of the stainless steel surface to liquid water, such as cooling water used during fuel cell operation or water generated during operation, can cause corrosion. Therefore, when using stainless steel substrates for fuel cell separators, there are areas where further improvement in corrosion resistance is necessary.
前記の通り、従来のステンレス製の燃料電池用セパレータの製造においては、耐食性の向上が求められることがあった。それ故、本発明は、耐食性をさらに向上した燃料電池用セパレータの製造方法を提供することを目的とする。 As mentioned above, in the manufacturing of conventional stainless steel fuel cell separators, there has been a need for improved corrosion resistance. Therefore, the present invention aims to provide a method for manufacturing fuel cell separators with further improved corrosion resistance.
本発明者らは、ステンレス基材の液水との接触面にレーザー処理を施すことにより、耐食性をさらに向上させることができることを見出し、本発明を完成した。 The inventors of this invention have discovered that the corrosion resistance of a stainless steel substrate can be further improved by applying laser treatment to the contact surface with liquid water, and have completed this invention.
すなわち、本発明の要旨は以下の通りである。
(1)ステンレス製の燃料電池用セパレータの製造方法であって、セパレータの形状に成形したステンレス基材の液水との接触面にレーザー処理を施し、ステンレス基材表面の不働態被膜を改質することを含み、
前記ステンレス基材表面のレーザー処理部の不働態被膜が、X線光電子分光法(XPS)によって求められる、
Cr含有量(Atomic%)のFe含有量(Atomic%)に対する比率(Cr/Fe比)が、レーザー処理前を1としたときに1超であり、及び/又は
Mn含有量(Atomic%)のFe含有量(Atomic%)に対する比率(Mn/Fe比)が、レーザー処理前を1としたときに1超である
不働態被膜に改質される、燃料電池用セパレータの製造方法。
(2)前記レーザーのエネルギー密度が10mJ/mm2~40mJ/mm2である、前記(1)に記載の燃料電池用セパレータの製造方法。
(3)前記レーザーのエネルギー密度が10mJ/mm2~20mJ/mm2である、前記(1)又は(2)に記載の燃料電池用セパレータの製造方法。
In other words, the gist of this invention is as follows:
(1) A method for manufacturing a stainless steel fuel cell separator, comprising applying laser treatment to the contact surface with liquid water of a stainless steel substrate formed into the shape of a separator, thereby modifying the passivation film on the surface of the stainless steel substrate,
The passivation film on the surface of the stainless steel substrate treated with the laser is determined by X-ray photoelectron spectroscopy (XPS).
A method for manufacturing a fuel cell separator, wherein the separator is modified into a passivation film in which the ratio of Cr content (atomic%) to Fe content (atomic%) (Cr/Fe ratio) is greater than 1 when the pre-laser treatment is set to 1, and/or the ratio of Mn content (atomic%) to Fe content (atomic%) (Mn/Fe ratio) is greater than 1 when the pre-laser treatment is set to 1.
(2) The method for manufacturing a fuel cell separator according to (1), wherein the energy density of the laser is 10 mJ/ mm² to 40 mJ/ mm² .
(3) The method for manufacturing a fuel cell separator according to (1) or (2), wherein the energy density of the laser is 10 mJ/ mm² to 20 mJ/ mm² .
本発明により、耐食性がさらに向上した燃料電池用セパレータの製造方法を提供することが可能となる。 This invention makes it possible to provide a method for manufacturing a fuel cell separator with further improved corrosion resistance.
以下、本発明の好ましい実施形態について詳細に説明する。 The following describes preferred embodiments of the present invention in detail.
本発明は、ステンレス基材からステンレス製の燃料電池用セパレータを製造する方法に関する。本発明の燃料電池用セパレータの製造方法は、セパレータの形状に成形したステンレス基材の液水(生成水や冷却水)との接触面、特にマニホールド周りにレーザー処理を施すことを含む。 This invention relates to a method for manufacturing a stainless steel fuel cell separator from a stainless steel substrate. The manufacturing method of the fuel cell separator according to this invention includes laser treatment of the contact surface of the stainless steel substrate, which has been molded into the shape of a separator, with the liquid water (generated water or cooling water), particularly around the manifold.
ステンレス基材のステンレスとしては、特に限定されずに、例えば、JIS G 4305:2015にて規定される、SUS304、SUS316及びSUS430等のオーステナイト系ステンレスや、SUS444等のフェライト系ステンレスが挙げられる。 The stainless steel used as the base material is not particularly limited, but examples include austenitic stainless steels such as SUS304, SUS316, and SUS430 as defined in JIS G 4305:2015, and ferritic stainless steels such as SUS444.
ステンレス基材の厚さは、特に限定されずに、通常80μm~200μmであり、好ましくは80μm~100μmである。 The thickness of the stainless steel substrate is not particularly limited, but is usually 80 μm to 200 μm, preferably 80 μm to 100 μm.
本発明においては、セパレータの形状に成形したステンレス基材の表面にレーザーを照射して、ステンレス基材表面の不働態被膜を改質する。ステンレス基材のセパレータの形状への成形は、例えば、プレス成形により行うことができる。セパレータの形状とは、通常の燃料電池用セパレータの形状であればよく、例えば、長手方向に沿って凹凸に多数の溝部が形成され、燃料ガス、酸化剤ガス及び冷媒の流路が形成された形状であるが、これらの流路を確保できればこの形状に限定されない。 In this invention, the passive coating on the surface of a stainless steel substrate, which has been molded into the shape of a separator, is modified by irradiating it with a laser. The stainless steel substrate can be molded into the separator shape, for example, by press molding. The separator shape can be any shape typical of a fuel cell separator; for example, a shape in which numerous grooves are formed along the longitudinal direction, creating passages for fuel gas, oxidizer gas, and refrigerant. However, it is not limited to this shape as long as these passages can be secured.
本発明においては、セパレータの形状に成形したステンレス基材の表面にレーザーを照射して、レーザーで処理した部位(レーザー処理部)の耐食性を向上させることができる。燃料電池用セパレータは、通常、燃料ガスや酸化剤ガスと接触するガス面側において液水として生成水と接触し、厚み方向に対してその反対側の冷却面側では液水として冷却水と接触する。特に燃料ガスと空気を流すマニホールド周囲は生成水が溜まりやすく、冷却水マニホールドは冷却水を電解液とした電気化学腐食が発生しやすい。本発明においては、ステンレス基材表面をレーザーで処理した部位では耐食性が向上するため、生成水と接触するマニホールド周囲の表面や、冷却水と接し電気化学腐食が生じる冷却水マニホールド周囲にレーザー処理を施すことが好ましい。本発明において、レーザー処理は、少なくともステンレス基材表面のマニホールド周りの液水と接触する部位に実施すればよいが、ステンレス基材の表面全体に実施してもよい。 In this invention, the corrosion resistance of the laser-treated portion (laser-treated area) can be improved by irradiating the surface of a stainless steel substrate molded into the shape of a separator with a laser. Fuel cell separators typically come into contact with generated water as liquid water on the gas side, which is in contact with fuel gas and oxidizer gas, and with cooling water as liquid water on the cooling side, which is opposite the gas side in the thickness direction. In particular, generated water tends to accumulate around the manifold through which fuel gas and air flow, and electrochemical corrosion is likely to occur in the cooling water manifold, where the cooling water acts as the electrolyte. In this invention, since the corrosion resistance is improved in the laser-treated portion of the stainless steel substrate surface, it is preferable to apply laser treatment to the surface around the manifold that comes into contact with generated water, and to the area around the cooling water manifold where electrochemical corrosion occurs due to contact with cooling water. In this invention, laser treatment only needs to be performed on the portion of the stainless steel substrate surface that comes into contact with liquid water around the manifold, but it may also be performed on the entire surface of the stainless steel substrate.
レーザー処理は、レーザーのエネルギー密度(以下、フルエンスとも記載する)と、処理速度が以下の式(1)を満たすように行うことが好ましい。
フルエンスE(mJ/mm2)/処理速度V(mm/s)=α 式(1)
(式(1)において、αは、好ましくは0.0033~0.0133であり、より好ましくは0.0033~0.0067であり、特に好ましくは0.0067である。)
Laser processing is preferably performed such that the laser energy density (hereinafter also referred to as fluence) and processing speed satisfy the following equation (1).
Fluence E (mJ/ mm² ) / Processing speed V (mm/s) = α Equation (1)
(In formula (1), α is preferably 0.0033 to 0.0133, more preferably 0.0033 to 0.0067, and particularly preferably 0.0067.)
レーザーのフルエンスは、好ましくは10mJ/mm2~40mJ/mm2であり、より好ましくは10mJ/mm2~20mJ/mm2又は20mJ/mm2超~40mJ/mm2であり、特に好ましくは10mJ/mm2~20mJ/mm2である。レーザーのフルエンスが10mJ/mm2~40mJ/mm2であると、レーザー処理前のステンレス基材表面の厚み数nmの不態被膜を溶解し、耐食性が高いCr及び/又はMnリッチな新たな不働態被膜を形成することができる。また、レーザーのフルエンスが10mJ/mm2~20mJ/mm2であると、よりCrとMnリッチな不働態被膜を形成することができるため、耐食性がさらに向上する。また、低エネルギーのためレーザー発振器の寿命が延びランニングコスト低減の点でも好ましい。 The laser fluence is preferably 10 mJ/ mm² to 40 mJ/ mm² , more preferably 10 mJ/ mm² to 20 mJ/ mm² or greater than 20 mJ/ mm² to 40 mJ/ mm² , and particularly preferably 10 mJ/ mm² to 20 mJ/ mm² . When the laser fluence is 10 mJ/ mm² to 40 mJ/ mm² , the passive film of several nanometers thickness on the surface of the stainless steel substrate before laser treatment can be dissolved, and a new passive film rich in Cr and/or Mn with high corrosion resistance can be formed. Furthermore, when the laser fluence is 10 mJ/ mm² to 20 mJ/ mm² , an even more Cr and Mn-rich passive film can be formed, further improving corrosion resistance. In addition, the low energy extends the life of the laser oscillator, which is also preferable in terms of reducing running costs.
レーザーの処理速度は、前記式(1)を満たすように選択すればよく、例えば1000mm/s~5000m/sであり、好ましくは2000mm/s~4000mm/sである。 The laser processing speed should be selected to satisfy equation (1) above, for example, 1000 mm/s to 5000 m/s, preferably 2000 mm/s to 4000 mm/s.
前記の本発明の製造方法により、レーザーで処理した部位の耐食性が向上した、ステンレス製の燃料電池用セパレータが得られる。本発明の製造方法により得られる燃料電池用セパレータは、レーザー処理により、ステンレス基材表面の不働態被膜が耐食性の向上した不働態被膜に改質されている。 The manufacturing method of the present invention provides a stainless steel fuel cell separator with improved corrosion resistance in the laser-treated areas. The fuel cell separator obtained by the manufacturing method of the present invention has a passive coating on the surface of the stainless steel substrate that has been modified by laser treatment to a passive coating with improved corrosion resistance.
本発明の製造方法により得られる燃料電池用セパレータにおいて、ステンレス基材表面のレーザー処理部の、クロム酸化物(一般にCr2O3)の不働態被膜の厚みは、好ましくは1nm~50nmであり、より好ましくは1nm~25nmである。レーザー処理部の不働態被膜の厚みは、レーザーのフルエンスによって変わる。例えば、レーザーのフルエンスが20mJ/mm2である場合、レーザー処理部の不働態被膜の厚みは、レーザー処理前と同等であり、通常1nm~3nm程度である。また、レーザーのフルエンスが30mJ/mm2である場合、レーザー処理部の不働態被膜の厚みは、レーザー処理前よりも増加し、通常15nm~25nm程度である。 In a fuel cell separator obtained by the manufacturing method of the present invention, the thickness of the passivation film of chromium oxide (generally Cr₂O₃ ) in the laser-treated area on the surface of the stainless steel substrate is preferably 1 nm to 50 nm , and more preferably 1 nm to 25 nm. The thickness of the passivation film in the laser-treated area varies depending on the laser fluence. For example, when the laser fluence is 20 mJ/ mm² , the thickness of the passivation film in the laser-treated area is the same as before laser treatment, and is usually about 1 nm to 3 nm. When the laser fluence is 30 mJ/ mm² , the thickness of the passivation film in the laser-treated area increases compared to before laser treatment, and is usually about 15 nm to 25 nm.
本発明の製造方法により得られる燃料電池用セパレータにおいて、ステンレス基材表面のレーザー処理部の不働態被膜は、X線光電子分光法(XPS)によって求められる、Cr含有量(Atomic%)のFe含有量(Atomic%)に対する比率(Cr/Fe比)が、レーザー処理前を1としたときに1超であり、及び/又はMn含有量(Atomic%)のFe含有量(Atomic%)に対する比率(Mn/Fe比)が、レーザー処理前を1としたときに1超である不働態被膜に改質されている。すなわち、ステンレス基材表面のレーザー処理部の不働態被膜は、Cr/Fe比及びMn/Fe比の少なくとも一方がレーザー処理前を1としたときに1超である不働態被膜に改質されている。 In the fuel cell separator obtained by the manufacturing method of the present invention, the passivation coating on the laser-treated surface of the stainless steel substrate is modified to a passivation coating in which the ratio of Cr content (atomic%) to Fe content (atomic%) (Cr/Fe ratio), determined by X-ray photoelectron spectroscopy (XPS), is greater than 1 when the pre-laser treatment ratio is set to 1, and/or the ratio of Mn content (atomic%) to Fe content (atomic%) (Mn/Fe ratio), is greater than 1 when the pre-laser treatment ratio is set to 1. In other words, the passivation coating on the laser-treated surface of the stainless steel substrate is modified to a passivation coating in which at least one of the Cr/Fe ratio and the Mn/Fe ratio is greater than 1 when the pre-laser treatment ratio is set to 1.
本発明の製造方法により得られる燃料電池用セパレータにおいて、XPS分析によって求められる、ステンレス基材表面のレーザー処理部の不働態被膜中のCr/Fe比は、レーザー処理前を1としたときに、通常0.7~3.0である。レーザー処理部の不働態被膜中のCr/Fe比は、レーザーのフルエンスによって変わる。例えば、レーザーのフルエンスが20mJ/mm2である場合、レーザー処理部の不働態被膜中のCr/Fe比は、レーザー処理前よりも増加する。すなわち、レーザー処理前を1としたときに1超である。また、レーザーのフルエンスが30mJ/mm2である場合、レーザー処理部の不働態被膜中のCr/Fe比は、レーザー処理前よりも低下する。すなわち、レーザー処理前を1としたときに1未満であるが、Mn/Feは1超である。 In fuel cell separators obtained by the manufacturing method of the present invention, the Cr/Fe ratio in the passivation film of the laser-treated surface of the stainless steel substrate, as determined by XPS analysis, is typically 0.7 to 3.0, with the value before laser treatment set to 1. The Cr/Fe ratio in the passivation film of the laser-treated surface changes depending on the laser fluence. For example, when the laser fluence is 20 mJ/ mm² , the Cr/Fe ratio in the passivation film of the laser-treated surface increases compared to before laser treatment. That is, it is greater than 1 when the value before laser treatment is set to 1. Also, when the laser fluence is 30 mJ/ mm² , the Cr/Fe ratio in the passivation film of the laser-treated surface decreases compared to before laser treatment. That is, it is less than 1 when the value before laser treatment is set to 1, but Mn/Fe is greater than 1.
一実施形態において、レーザーのフルエンスが20mJ/mm2である場合、本発明の製造方法により得られる燃料電池用セパレータにおいて、ステンレス基材表面のレーザー処理部の不働態被膜の厚みは、レーザー処理前と同等であり、通常1nm~3nm程度であり、且つ不働態被膜中のCr/Fe比とMn/Fe比は、レーザー処理前よりも増加する(すなわち、レーザー処理前を1としたときに1超である)。この実施形態においては、レーザー処理部の不働態被膜の厚みはレーザー処理前と同等であるが、不働態被膜中のCr/Fe比とMn/Fe比が有意に増加する。すなわち、不働態被膜がよりCrとMnリッチな酸化物で構成されることにより被膜中のFe化合物が相対的に減少し、レーザー処理部の耐食性が向上すると推測される。 In one embodiment, when the laser fluence is 20 mJ/ mm² , the thickness of the passivation film in the laser-treated area of the stainless steel substrate separator obtained by the manufacturing method of the present invention is the same as before laser treatment, typically around 1 nm to 3 nm, and the Cr/Fe ratio and Mn/Fe ratio in the passivation film increase compared to before laser treatment (i.e., greater than 1 when the value before laser treatment is set to 1). In this embodiment, although the thickness of the passivation film in the laser-treated area is the same as before laser treatment, the Cr/Fe ratio and Mn/Fe ratio in the passivation film increase significantly. That is, it is presumed that the Fe compound in the film is relatively reduced because the passivation film is composed of more Cr and Mn-rich oxides, and the corrosion resistance of the laser-treated area is improved.
別の一実施形態において、レーザーのフルエンスが30mJ/mm2である場合、本発明の製造方法により得られる燃料電池用セパレータにおいて、ステンレス基材表面のレーザー処理部の不働態被膜の厚みは、レーザー処理前よりも増加し、通常15nm~25nm程度であり、且つ不働態被膜中のCr/Fe比は、レーザー処理前よりも低下し(すなわち、レーザー処理前を1としたときに1未満である)、不働態被膜中のMn/Fe比は、レーザー処理前よりも増加する(すなわち、レーザー処理前を1としたときに1超である)。この実施形態においては不働態被膜がCrリッチな酸化物ではないものの、不働態被膜の厚みがさらに厚くなることとMn/Fe比の向上により、レーザー処理部の耐食性が向上したと推測される。このように、本発明においては、不働態被膜中のMn/Fe比の向上も耐食性の向上に重要である。 In another embodiment, when the laser fluence is 30 mJ/ mm² , in the fuel cell separator obtained by the manufacturing method of the present invention, the thickness of the passivation film in the laser-treated area on the surface of the stainless steel substrate increases compared to before laser treatment, and is typically about 15 nm to 25 nm. Furthermore, the Cr/Fe ratio in the passivation film decreases compared to before laser treatment (i.e., it is less than 1 when the value before laser treatment is set to 1), and the Mn/Fe ratio in the passivation film increases compared to before laser treatment (i.e., it is greater than 1 when the value before laser treatment is set to 1). In this embodiment, although the passivation film is not a Cr-rich oxide, it is presumed that the corrosion resistance of the laser-treated area is improved due to the further increase in the thickness of the passivation film and the improvement in the Mn/Fe ratio. Thus, in the present invention, improving the Mn/Fe ratio in the passivation film is also important for improving corrosion resistance.
本発明の燃料電池用セパレータは、レーザー処理により、腐食環境における耐食性を向上させることができる。本発明において、腐食環境とは、例えば、0.8V~1.0Vの電位をかけた70℃~100℃以下の模擬生成水(pH=3~5)に24時間(hr)以上セパレータを浸漬させるような条件をいう。 The fuel cell separator of the present invention can have its corrosion resistance in corrosive environments improved by laser treatment. In this invention, a corrosive environment refers to conditions such as immersing the separator in simulated generated water (pH = 3-5) at a temperature of 70°C to 100°C with a potential of 0.8V to 1.0V for 24 hours (hr) or more.
本発明の燃料電池用セパレータは、前記腐食環境において、XPS分析によって求められる、ステンレス基材表面のレーザー処理部の不働態被膜中のCr/Fe比が経時的に増加する。一方、レーザー未処理部では、不働態被膜中のCr/Fe比は経時的に低下する。本発明の燃料電池用セパレータの製造方法では、レーザー処理を施すことにより、得られる燃料電池用セパレータの腐食環境における耐食性の強度が高まり、腐食環境においても腐食が全く進まないようにすることができる。 In the fuel cell separator of the present invention, the Cr/Fe ratio in the passivation film of the laser-treated surface of the stainless steel substrate, as determined by XPS analysis, increases over time in the aforementioned corrosive environment. Conversely, in the untreated surface, the Cr/Fe ratio in the passivation film decreases over time. In the manufacturing method of the fuel cell separator of the present invention, by applying laser treatment, the corrosion resistance of the resulting fuel cell separator in a corrosive environment is increased, and corrosion can be prevented entirely even in a corrosive environment.
以下、実施例を用いて本発明をさらに具体的に説明する。但し、本発明の技術的範囲はこれら実施例に限定されるものではない。 The present invention will be described in more detail below using examples. However, the technical scope of the present invention is not limited to these examples.
<腐食試験>
ステンレス基材としてSUS304基材を用いた。SUS304基材の表面の一部に、エネルギー密度(フルエンス)20mJ/mm2又は30mJ/mm2、処理速度3000mm/sのレーザー処理を施して評価サンプルを得た。
<Corrosion Test>
SUS304 stainless steel was used as the substrate. A portion of the surface of the SUS304 substrate was subjected to laser treatment with an energy density (fluence) of 20 mJ/ mm² or 30 mJ/ mm² and a processing speed of 3000 mm/s to obtain evaluation samples.
評価サンプルについて、生成水を想定した腐食環境で定電位腐食試験を実施した。具体的には、評価サンプルを0.8V~1.0Vの電位をかけた70℃~100℃以下の模擬生成水(pH=3)に60時間浸漬させた。腐食試験後の腐食(変色)の有無を目視により確認した。 For the evaluation samples, a constant potential corrosion test was conducted in a corrosive environment simulating the generated water. Specifically, the evaluation samples were immersed for 60 hours in simulated generated water (pH=3) at a temperature of 70°C to 100°C with a potential of 0.8V to 1.0V. The presence or absence of corrosion (discoloration) after the corrosion test was visually confirmed.
腐食試験において、20mJ/mm2及び30mJ/mm2のいずれのフルエンスの評価サンプルにおいても、レーザー処理部は変色しておらず、腐食が認められなかったが、レーザー未処理部は、茶色~紫色に変色し、腐食が認められた。よって、レーザー処理によりSUS304基材の耐食性が向上することが確認された。なお、レーザー未処理部の腐食の色(茶色~紫色)の違いは、SUS304基材表面の不働態被膜の厚みや組成のばらつきによるものと考えられる。 In corrosion tests, the laser-treated samples showed no discoloration and no corrosion in either the 20 mJ/ mm² or 30 mJ/ mm² fluence evaluation samples. However, the untreated samples showed discoloration ranging from brown to purple, indicating corrosion. Therefore, it was confirmed that laser treatment improves the corrosion resistance of the SUS304 substrate. The difference in corrosion color (brown to purple) in the untreated samples is thought to be due to variations in the thickness and composition of the passive film on the surface of the SUS304 substrate.
<耐食性向上のメカニズム解析>
腐食試験において確認された耐食性向上のメカニズム解析のために、腐食試験前後の評価サンプルに対して、SUS304基材表面の不働態被膜の表面と深さ方向の元素についてX線光電子分光法(XPS)分析を実施した。XPS分析は、XPS装置(ULVAC製;PHI5000 VersaProbeII)を用いて、以下の条件:X線源;AlKα単色光、出力25W、電圧15kV、照射範囲;φ100μm、分析範囲;1000×200μm、中和銃;ON状態、パルスエネルギーは(ワイド;187.85eV、ナロー;46.95-117.40eV)、ステップ幅は(ワイド;0.4eV、ナロー;0.1eV)、シフト補正はC1s;C-C,C-H、284.8eVで実施し、デプス分析は、Arモノマーでエッチングしながら、電圧は3kV、照射面積は2×2mm、堀込速度(スパッタ速度)は6.5nm/minで実施した。
<Analysis of the mechanism for improving corrosion resistance>
To analyze the mechanism of improved corrosion resistance confirmed in corrosion tests, X-ray photoelectron spectroscopy (XPS) analysis was performed on evaluation samples before and after the corrosion tests to analyze the elements in the surface and depth directions of the passivation film on the SUS304 substrate surface. XPS analysis was performed using an XPS instrument (ULVAC; PHI5000 VersaProbeII) under the following conditions: X-ray source; AlKα monochromatic light, output 25W, voltage 15kV, irradiation area; φ100μm, analysis area; 1000×200μm, neutralization gun; ON state, pulse energy (wide; 187.85 eV, narrow; 46.95-117.40 eV), step size (wide; 0.4 eV, narrow; 0.1 eV), shift correction C1s; C-C, C-H, 284.8 eV. Depth analysis was performed while etching with Ar monomer at a voltage of 3kV, irradiation area of 2×2 mm, and etching speed (sputtering speed) of 6.5 nm/min.
1.腐食試験前の不働態被膜の表面分析
1-1.腐食試験前の不働態被膜最表面の元素分析
腐食試験前の不働態被膜最表面の元素分析結果を表1に示す。表1に示されるように、低フルエンスの20mJ/mm2レーザー処理部では、レーザー未処理部に対して、Cr量とMn量が増加し、Fe量が減少していた。一方、高フルエンスの30mJ/mm2レーザー処理部では、レーザー未処理部に対して、Cr量が減少し、Fe量、Mn量、O量が増加していた。レーザー処理部のCr/Fe比は、低フルエンスの20mJ/mm2ではレーザー未処理部よりも高いが、高フルエンスの30mJ/mm2では未処理部より低かった。一方、Mn/Fe比は、フルエンスによらず、レーザー処理部は未処理部より高かった。Mn/Fe比が向上することは、酸素と結合するFe量が不働態被膜中で相対的に減少していることを表すため、これも耐食性向上に寄与していると考えられる。
1. Surface Analysis of Passivation Film Before Corrosion Testing 1-1. Elemental Analysis of the Outer Surface of Passivation Film Before Corrosion Testing Table 1 shows the results of the elemental analysis of the outer surface of the passivation film before corrosion testing. As shown in Table 1, in the low-fluence 20 mJ/ mm² laser treatment area, the amount of Cr and Mn increased and the amount of Fe decreased compared to the untreated area. On the other hand, in the high-fluence 30 mJ/ mm² laser treatment area, the amount of Cr decreased and the amount of Fe, Mn, and O increased compared to the untreated area. The Cr/Fe ratio of the laser-treated area was higher than that of the untreated area at the low-fluence 20 mJ/ mm² , but lower at the high-fluence 30 mJ/ mm² . On the other hand, the Mn/Fe ratio was higher in the laser-treated area than in the untreated area, regardless of fluence. An improvement in the Mn/Fe ratio indicates that the amount of Fe that binds with oxygen is relatively reduced in the passivated coating, and this is also thought to contribute to improved corrosion resistance.
1-2.腐食試験前の不働態被膜の深さ方向の分析
図1A~Cに、腐食試験前の不働態被膜の深さ方向のXPS分析(スパッタ速度:6.5nm/min)の結果を示す(図1A:20mJ/mm2レーザー処理部、図1B:30mJ/mm2レーザー処理部、図1C:レーザー未処理部)。図1A~Cから不働態被膜(≒酸化被膜)の厚みを求めた。具体的には、不働態被膜の厚みは一般に最大O量(酸素量)の1/2で定義されるので、これに基づいて、グラフの横軸(スパッタ時間)の数値を換算して不働態被膜の厚みを計算した(図1A~C中、折れ線の矢印で示す)。その結果、レーザーフルエンス20mJ/mm2では、不働態被膜の厚みは約2.3nmであり(図1A)、レーザーフルエンス30mJ/mm2では、不働態被膜の厚みは約19.5nmとかなり厚みが増しており(図1B)、レーザー未処理部の不働態被膜の厚みは約2.0nmであり(図1C)、一般的に言われるステンレスの不働態被膜の厚み(1~2nm)に一致していた。
1-2. Analysis of the passivation film in the depth direction before corrosion testing Figures 1A to C show the results of XPS analysis (sputtering rate: 6.5 nm/min) of the passivation film in the depth direction before corrosion testing (Figure 1A: 20 mJ/ mm² laser treatment, Figure 1B: 30 mJ/ mm² laser treatment, Figure 1C: untreated). The thickness of the passivation film (≒ oxide film) was determined from Figures 1A to C. Specifically, the thickness of the passivation film is generally defined as half of the maximum O amount (oxygen amount), so the thickness of the passivation film was calculated by converting the values on the horizontal axis (sputtering time) of the graph based on this (indicated by the line arrows in Figures 1A to C). As a result, at a laser fluence of 20 mJ/ mm² , the thickness of the passivation film was approximately 2.3 nm (Figure 1A), and at a laser fluence of 30 mJ/ mm² , the thickness of the passivation film increased considerably to approximately 19.5 nm (Figure 1B). The thickness of the passivation film in the untreated area was approximately 2.0 nm (Figure 1C), which was consistent with the generally accepted thickness of the passivation film on stainless steel (1-2 nm).
これらのことから、低フルエンスの20mJ/mm2レーザー処理部では、不働態被膜の厚みはレーザー未処理部とほぼ同等であるにもかかわらず耐食性が向上していることが分かった。図2Aに示される腐食試験前の不働態被膜におけるCrの結合状態を表すXPSスペクトル、及び図2Bに示される腐食試験前の不働態被膜におけるOの結合状態を表すXPSスペクトルから分かるように、20mJ/mm2レーザー処理部では、未処理部に比べて、CrとOスペクトルがCr2O3のレンジでシャープであることから、不働態被膜がよりCrリッチな酸化物で構成されており、このため耐食性が向上したと推測される。30mJ/mm2レーザー処理部では、不働態被膜中のCr量は少ないが、20mJ/mm2レーザー処理部と同様にCrとOスペクトルがCr2O3のレンジでシャープであることと、不働態被膜の厚みが厚いことが耐食性の向上に寄与していると推測される。このように、不働態被膜におけるCr、Oの結合状態を表すXPSスペクトルにおいて、CrとOの強度がCr2O3の領域でシャープな形状であることが耐食性の向上に重要であると考えられる。 From these findings, it was found that in the low-fluence 20 mJ/ mm² laser treatment area, corrosion resistance was improved despite the passivation film thickness being almost the same as in the untreated area. As can be seen from the XPS spectrum representing the Cr bonding state in the passivation film before corrosion testing shown in Figure 2A, and the XPS spectrum representing the O bonding state in the passivation film before corrosion testing shown in Figure 2B, in the 20 mJ/ mm² laser treatment area, the Cr and O spectra are sharper in the Cr₂O₃ range compared to the untreated area. This suggests that the passivation film is composed of a more Cr-rich oxide, which is likely the reason for the improved corrosion resistance. In the 30 mJ/ mm² laser treatment area, although the amount of Cr in the passivation film is small, it is presumed that the sharpness of the Cr and O spectra in the Cr₂O₃ range, similar to the 20 mJ/ mm² laser treatment area, and the thicker passivation film, contribute to the improved corrosion resistance. Thus, in the XPS spectrum representing the bonding state of Cr and O in the passivation film, it is considered important for the intensity of Cr and O to be sharp in the Cr2O3 region to improve corrosion resistance.
2.腐食試験後の不働態被膜の表面分析
2-1.腐食試験後の不働態被膜最表面の元素分析
腐食試験後の不働態被膜最表面の元素分析結果を表2に示す。表2に示されるように、レーザーフルエンスによらず、レーザー処理部は未処理部(腐食部)に比べてFe量が少なく、Cr量が多かった。図3A~Cに、レーザー処理部と未処理部の腐食試験時間毎のCr/Fe比の変化を示す(図3A:20mJ/mm2レーザー処理部、図3B:30mJ/mm2レーザー処理部、図3C:レーザー未処理部)。図3A及びBより、レーザー処理部では腐食試験時間とともにCr/Fe比が増加していた。これは、レーザー処理部では、生成水と接するような腐食環境において耐食性の強度が高まる(すなわち、腐食が全く進まない)ことを意味する。一方、図3Cより、レーザー未処理部(SUS304基材)では、初期(腐食試験前、0hr)の不働態被膜表面のCr/Fe比に対して、腐食試験時間とともにCr/Fe比は低下し、いずれゼロになる傾向を示した。これは、レーザー処理による不働態被膜の改質をしていないステンレス基材のままでは耐食性が悪化していくことを意味する。
2. Surface Analysis of Passivated Coating After Corrosion Test 2-1. Elemental Analysis of the Outer Surface of the Passivated Coating After Corrosion Test Table 2 shows the results of the elemental analysis of the outer surface of the passivated coating after the corrosion test. As shown in Table 2, regardless of the laser fluence, the laser-treated area had less Fe and more Cr compared to the untreated (corroded) area. Figures 3A to 3C show the change in the Cr/Fe ratio for each corrosion test time in the laser-treated and untreated areas (Figure 3A: 20 mJ/ mm² laser-treated area, Figure 3B: 30 mJ/ mm² laser-treated area, Figure 3C: untreated area). From Figures 3A and 3B, the Cr/Fe ratio increased with corrosion test time in the laser-treated area. This means that in the laser-treated area, the corrosion resistance strength increases in corrosive environments such as contact with generated water (i.e., corrosion does not progress at all). On the other hand, as shown in Figure 3C, in the untreated SUS304 substrate, the Cr/Fe ratio on the passive coating surface decreased with the corrosion test time compared to the initial (before corrosion test, 0 hr) Cr/Fe ratio, eventually showing a tendency to become zero. This means that the corrosion resistance deteriorates if the stainless steel substrate is left as is without modification of the passive coating by laser treatment.
2-2.腐食試験後の不働態被膜の深さ方向の分析
前記2-1の結果を不働態被膜の深さ方向のXPS分析で確認した。図4A及びBに、腐食試験後のレーザー処理部の不働態被膜の深さ方向のXPS分析(スパッタ速度:6.5nm/min)の結果を示す(図4A:20mJ/mm2レーザー処理部、図4B:30mJ/mm2レーザー処理部)。また、図5A及びBに、腐食試験後のレーザー未処理部(腐食部)の不働態被膜の深さ方向のXPS分析(スパッタ速度:6.5nm/min)の結果を示す(図5A:20mJ/mm2レーザー処理サンプルの未処理部、図5B:30mJ/mm2レーザー処理サンプルの未処理部)。図4A及びBより、レーザー処理部ではCrリッチ層が増加し、不働態被膜の厚みが増加しているのに対し(図4A及びB中、折れ線の矢印(I)及び(II)で示す)、図5A及びBより、レーザー未処理部はCrがほとんど存在しない酸化被膜に変化していた。図6Aに示される腐食試験後の不働態被膜におけるCrの結合状態を表すXPSスペクトル、及び図6Bに示される腐食試験後の不働態被膜におけるOの結合状態を表すXPSスペクトルから分かるように、レーザー処理部ではCr2O3の不働態被膜であるのに対して、レーザー未処理部ではFe2O3主体の酸化被膜に変化していた。
2-2. Depth-direction analysis of the passivation film after corrosion testing The results of 2-1 above were confirmed by XPS analysis of the passivation film in the depth direction. Figures 4A and 4B show the results of XPS analysis of the passivation film in the depth direction (sputtering rate: 6.5 nm/min) of the laser-treated area after corrosion testing (Figure 4A: 20 mJ/ mm² laser-treated area, Figure 4B: 30 mJ/ mm² laser-treated area). Figures 5A and 5B also show the results of XPS analysis of the passivation film in the depth direction (sputtering rate: 6.5 nm/min) of the untreated area (corroded area) after corrosion testing (Figure 5A: untreated area of the 20 mJ/ mm² laser-treated sample, Figure 5B: untreated area of the 30 mJ/ mm² laser-treated sample). From Figures 4A and 4B, the Cr-rich layer increased and the thickness of the passive film increased in the laser-treated area (indicated by the broken line arrows (I) and (II) in Figures 4A and 4B), whereas from Figures 5A and 5B, the untreated area had changed into an oxide film with almost no Cr. As can be seen from the XPS spectra representing the Cr bonding state in the passive film after the corrosion test shown in Figure 6A, and the XPS spectra representing the O bonding state in the passive film after the corrosion test shown in Figure 6B , the laser-treated area had a Cr₂O₃ passive film, while the untreated area had changed into an oxide film mainly composed of Fe₂O₃ .
Claims (3)
前記ステンレス基材表面のレーザー処理部の不働態被膜が、X線光電子分光法(XPS)によって求められる、
Cr含有量(Atomic%)のFe含有量(Atomic%)に対する比率(Cr/Fe比)が、レーザー処理前を1としたときに1超であり、及び/又は
Mn含有量(Atomic%)のFe含有量(Atomic%)に対する比率(Mn/Fe比)が、レーザー処理前を1としたときに1超である
不働態被膜に改質される、燃料電池用セパレータの製造方法。 A method for manufacturing a stainless steel fuel cell separator, comprising applying laser treatment to the contact surface with liquid water of a stainless steel substrate formed into the shape of a separator, thereby modifying the passivation film on the surface of the stainless steel substrate.
The passivation film on the surface of the stainless steel substrate treated with the laser is determined by X-ray photoelectron spectroscopy (XPS).
A method for manufacturing a fuel cell separator, wherein the separator is modified into a passivation film in which the ratio of Cr content (atomic%) to Fe content (atomic%) (Cr/Fe ratio) is greater than 1 when the pre-laser treatment is set to 1, and/or the ratio of Mn content (atomic%) to Fe content (atomic%) (Mn/Fe ratio) is greater than 1 when the pre-laser treatment is set to 1.
The method for manufacturing a fuel cell separator according to claim 1 or 2, wherein the energy density of the laser is 10 mJ/ mm² to 20 mJ/ mm² .
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Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002042827A (en) | 2000-07-28 | 2002-02-08 | Shinko Pantec Co Ltd | Fuel cell separator, method of manufacturing the same, and fuel cell |
| JP2004149920A (en) | 2002-10-07 | 2004-05-27 | Jfe Steel Kk | Stainless steel for polymer electrolyte fuel cell separator, method for producing the same, and polymer electrolyte fuel cell using the stainless steel |
| JP2005183338A (en) | 2003-12-24 | 2005-07-07 | Honda Motor Co Ltd | Fuel cell |
| JP2008027742A (en) | 2006-07-21 | 2008-02-07 | Sumitomo Metal Ind Ltd | Performance recovery method for stainless steel separator of polymer electrolyte fuel cell |
| JP2017210636A (en) | 2016-05-24 | 2017-11-30 | キヤノンマシナリー株式会社 | Coating film formation method |
| WO2018147087A1 (en) | 2017-02-09 | 2018-08-16 | Jfeスチール株式会社 | Stainless steel plate substrate of steel plate for fuel cell separator, and method for producing same |
| JP2021130850A (en) | 2020-02-20 | 2021-09-09 | 日鉄ステンレス株式会社 | Stainless steel, contact member, and manufacturing method of stainless steel |
| JP7244704B1 (en) | 2022-07-11 | 2023-03-22 | 日鉄テックスエンジ株式会社 | Method for improving corrosion resistance of stainless steel |
-
2023
- 2023-05-11 JP JP2023078737A patent/JP7831391B2/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002042827A (en) | 2000-07-28 | 2002-02-08 | Shinko Pantec Co Ltd | Fuel cell separator, method of manufacturing the same, and fuel cell |
| JP2004149920A (en) | 2002-10-07 | 2004-05-27 | Jfe Steel Kk | Stainless steel for polymer electrolyte fuel cell separator, method for producing the same, and polymer electrolyte fuel cell using the stainless steel |
| JP2005183338A (en) | 2003-12-24 | 2005-07-07 | Honda Motor Co Ltd | Fuel cell |
| JP2008027742A (en) | 2006-07-21 | 2008-02-07 | Sumitomo Metal Ind Ltd | Performance recovery method for stainless steel separator of polymer electrolyte fuel cell |
| JP2017210636A (en) | 2016-05-24 | 2017-11-30 | キヤノンマシナリー株式会社 | Coating film formation method |
| WO2018147087A1 (en) | 2017-02-09 | 2018-08-16 | Jfeスチール株式会社 | Stainless steel plate substrate of steel plate for fuel cell separator, and method for producing same |
| JP2021130850A (en) | 2020-02-20 | 2021-09-09 | 日鉄ステンレス株式会社 | Stainless steel, contact member, and manufacturing method of stainless steel |
| JP7244704B1 (en) | 2022-07-11 | 2023-03-22 | 日鉄テックスエンジ株式会社 | Method for improving corrosion resistance of stainless steel |
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