JP6581032B2 - ハニカム構造体 - Google Patents
ハニカム構造体 Download PDFInfo
- Publication number
- JP6581032B2 JP6581032B2 JP2016072586A JP2016072586A JP6581032B2 JP 6581032 B2 JP6581032 B2 JP 6581032B2 JP 2016072586 A JP2016072586 A JP 2016072586A JP 2016072586 A JP2016072586 A JP 2016072586A JP 6581032 B2 JP6581032 B2 JP 6581032B2
- Authority
- JP
- Japan
- Prior art keywords
- zeolite
- honeycomb structure
- volume
- inorganic binder
- coarse
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J29/00—Catalysts comprising molecular sieves
- B01J29/82—Phosphates
- B01J29/84—Aluminophosphates containing other elements, e.g. metals, boron
- B01J29/85—Silicoaluminophosphates [SAPO compounds]
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/0407—Constructional details of adsorbing systems
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- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
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- B01D53/8621—Removing nitrogen compounds
- B01D53/8625—Nitrogen oxides
- B01D53/8628—Processes characterised by a specific catalyst
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Crystallography & Structural Chemistry (AREA)
- Ceramic Engineering (AREA)
- Environmental & Geological Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Structural Engineering (AREA)
- Combustion & Propulsion (AREA)
- Thermal Sciences (AREA)
- Physics & Mathematics (AREA)
- Catalysts (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
Description
[9] 前記[1]〜[8]のいずれかに記載のハニカム構造体の製造方法であって、前記ゼオライト材料が、前記ゼオライト材料の総体積中に、前記無機結合材を3体積%以上含み、前記無機結合材が、塩基性乳酸アルミニウム由来のアルミナを、前記ゼオライト材料の総体積に対して1体積%以上含む、ハニカム構造体の製造方法。
[10] 前記無機結合材が、塩基性乳酸アルミニウム由来のアルミナと、ベーマイト由来のアルミナと、を含み、前記ベーマイト由来のアルミナの体積A2に対する、前記塩基性乳酸アルミニウム由来のアルミナの体積A1の比率であるA1/A2の値が、0.6以上である、前記[9]に記載のハニカム構造体の製造方法。
図1〜図3に示すように、本発明のハニカム構造体の一の実施形態は、粗粒ゼオライト、微粒ゼオライト、及び無機結合材を少なくとも含有するゼオライト材料から構成されたハニカム構造部4を含む、ハニカム構造体100である。ハニカム構造部4は、第一の端面11から第二の端面12まで延びる流体の流路となる複数のセル2を区画形成する隔壁1を有するものである。本実施形態のハニカム構造体100は、例えば、上述したゼオライト粒子と無機結合材とを少なくとも含有するゼオライト原料を押出成形して形成されたハニカム構造体100であることが好ましい。
式(1):無機結合材の体積の比率={(無機結合材の体積)/(ゼオライト粒子全体の体積+無機結合材の体積+その他の成分の体積)}
式(2):気孔率=細孔容量/(細孔容量+1/ハニカム構造部の真密度)×100
次に、本発明のハニカム構造体の製造方法について説明する。
粗粒ゼオライトとして、銅イオンで4.1質量%イオン交換された、平均粒子径が3.9μmのSAPO−34を用意した。また、微粒ゼオライトとして、銅イオンで6.3質量%イオン交換された、平均粒子径が0.4μmのβ型ゼオライトを用意した。表1に、実施例1に使用した粗粒ゼオライト及び微粒ゼオライトの種類及び平均粒子径を示す。表1の「ゼオライトの欄」の、「Cu−SAPO−34」は、銅イオンでイオン交換されたSAPO−34であることを意味する。また、表1の「ゼオライトの欄」の、「Cu−β」は、銅イオンでイオン交換されたβ型ゼオライトであることを意味する。各ゼオライトの平均粒子径は、それぞれのゼオライトの粒子を含有する粉末の粒子径分布におけるメジアン径(d50)であり、JIS R1629に準拠したレーザー回折散乱法にて測定した。
(2)ゼオライト材料全体の体積に対する、塩基性乳酸アルミニウム由来のアルミナの体積の比率(体積%)。
(3)ゼオライト材料全体の体積に対する、無機結合材の体積の比率(体積%)。
(4)ベーマイト由来のアルミナの体積A2に対する、塩基性乳酸アルミニウム由来のアルミナの体積A1の比率(A1/A2)。
(5)細孔径が0.02〜0.15μmの細孔容積比率(%)。
(6)細孔径0.02μm以下の細孔容積比率(%)。
(7)細孔径0.15μm以上の細孔容積比率(%)。
(8)細孔径0.52μm以上の細孔容積比率(%)。
(9)気孔率(%)。
(10)圧縮強度(MPa)。
式(3):気孔率=細孔容量/(細孔容量+1/ハニカム構造部の真密度)×100
表2に示すように、ゼオライト原料の配合処方を変更した以外は、実施例1と同様の方法で、ハニカム構造体を製造した。なお、実施例2〜8において、乳酸アルミニウムについては、乳酸アルミニウムの質量の2倍の質量の水に溶解して用いた。
粗粒ゼオライトとして、銅イオンで5.0質量%イオン交換された、平均粒子径が4.4μmのチャバサイトを用いた以外は実施例3と同様の配合と方法で、ハニカム構造体を製造した。
微粒ゼオライトとして銅イオンで5.0質量%イオン交換された、平均粒子径が0.6μmのチャバサイトを用いた以外は実施例9と同様の配合と方法で、ハニカム構造体を製造した。
表3に示すように、ゼオライト原料の配合処方を変更した以外は、実施例1と同様の方法で、ハニカム構造体を製造した。なお、比較例1、3及び5〜7においては、無機結合材として、アルミナゾルを用いた。アルミナゾルは、日産化学社製のアルミナゾル「AS520(商品名)」を用いた。
表4に示すように、実施例1〜10のハニカム構造体は、細孔径が0.02〜0.15μmの細孔容積比率が、42体積%以下であり、圧縮強度(MPa)が高いものであった。また、実施例1〜10のハニカム構造体は、ゼオライト材料中に粗粒ゼオライトとしてのチャバサイト型ゼオライトを含むものであるため、NOx浄化性能に優れたものであった。実施例1〜10のハニカム構造体は、無機結合材の凝集性が向上し、圧縮強度が向上したものと考えられる。また、図8に示すSEM画像においては、ゼオライト材料中のゼオライト粒子の輪郭が比較的に明瞭に確認することができた。即ち、このようなゼオライト材料は、ゼオライト材料中の無機結合材の凝集性が高く、無機結合材によって比較的緻密なネック部が形成され、その圧縮強度が高いものになっていると考えられる。
Claims (10)
- 平均粒子径が大きな粗粒ゼオライト、前記粗粒ゼオライトよりも平均粒子径が小さな微粒ゼオライト及び、無機結合材を少なくとも含有するゼオライト材料から構成されたハニカム構造部を含み、
前記粗粒ゼオライトは、一次粒子の平均粒子径が2μm以上、6μm以下のチャバサイト型ゼオライトであり、
前記微粒ゼオライトは、一次粒子の平均粒子径が0.02μm以上、2μm未満のものであり、
前記ハニカム構造部を構成する前記ゼオライト材料は、細孔径が0.02〜0.15μmの細孔の容積が、全細孔の容積に対して42%以下である、ハニカム構造体。 - 前記ゼオライト材料は、細孔径が0.02μm未満の細孔の容積が、全細孔の容積に対して8〜20%のものである、請求項1に記載のハニカム構造体。
- 前記ゼオライト材料は、細孔径が0.15μmを超える細孔の容積が、全細孔の容積の40〜60%で、且つ、細孔径が0.52μm以上の細孔の容積が、全細孔の容積の5%以下のものである、請求項1又は2に記載のハニカム構造体。
- 前記粗粒ゼオライト及び前記微粒ゼオライトが、イオン交換部位に銅イオンを含むものである、請求項1〜3のいずれか一項に記載のハニカム構造体。
- 前記粗粒ゼオライトが、チャバサイト、SAPO−34、及びSSZ−13のうち少なくとも一種のゼオライトである、請求項1〜4のいずれか一項に記載のハニカム構造体。
- 前記微粒ゼオライトが、β型ゼオライト、Y型ゼオライト、ZSM−5型ゼオライト、及びチャバサイト型ゼオライトのうち少なくとも一種のゼオライトである、請求項1〜5のいずれか一項に記載のハニカム構造体。
- 前記ゼオライト材料が、アルミナ繊維、シリカアルミナ繊維、及びガラス繊維のうちの少なくとも一種の無機繊維を含む、請求項1〜6のいずれか一項に記載のハニカム構造体。
- 前記ゼオライト材料が、前記ゼオライト材料の総体積中に、前記無機繊維を3〜8体積%含む、請求項7に記載のハニカム構造体。
- 請求項1〜8のいずれか一項に記載のハニカム構造体の製造方法であって、
前記ゼオライト材料が、前記ゼオライト材料の総体積中に、前記無機結合材を3体積%以上含み、
前記無機結合材が、塩基性乳酸アルミニウム由来のアルミナを、前記ゼオライト材料の総体積に対して1体積%以上含む、ハニカム構造体の製造方法。 - 前記無機結合材が、塩基性乳酸アルミニウム由来のアルミナと、ベーマイト由来のアルミナと、を含み、
前記ベーマイト由来のアルミナの体積A2に対する、前記塩基性乳酸アルミニウム由来のアルミナの体積A1の比率であるA1/A2の値が、0.6以上である、請求項9に記載のハニカム構造体の製造方法。
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