CATALISES

  • AGO-0X5L Catalyst mo PA Gaosiga mai le 0-xylene

    AGO-0X5L Catalyst mo PA Gaosiga mai le 0-xylene

    Fa'atasiga o vaila'au

    V-Tl u'amea u'amea fa'apipi'i i luga o le va'ava'a

    Meatotino Faaletino 

    Fa'ailoga Fa'ata

    mama gaogao masani

    Laisene Catalyst

    7.0*7.0*3.7±0.1mm

    To'atele Tele

    1.07±0.5kg/L

    Numera o Laega

    5

    Fa'atinoga Fa'atino

    O'osa'ina Gaua'i

    113-115wt% ina ua uma le tausaga muamua

    112-114wt% ina ua uma le tausaga lona lua

    110-112wt% pe a uma le tolu tausaga

    Vevelave Vevela

    400-440℃(Toe masani)

    Catalyst Pressure Pa'u

    0.20-0.25 Pa(G)

    Catalyst Lifetime

    > 3 tausaga

    Tulaga Fa'aaogā La'au Fa'atau 

    Tafe o le Ea

    4. 0NCM/tupa/h

    O-xylene uta

    320g/tu'u/h (Masa)

    400g/pa'u/h(Max)

    0-xylene fa'atonuga

    80g/NCM (Toe masani)

    100g/NCM (Max)

    Masima Masima

    350-375 ℃

    (E tusa ai ma tulaga o la'au a le tagata o tausia)

    Oloa Faiga ma Auaunaga

    AGO-0X5L, o le numera o lapisi faʻapipiʻi e 5 laulau, lea e atiaʻe ma faʻamalosia e faʻavae i luga o le phthalic ma le hydride catalyst technology i Europa. O lenei ituaiga o faʻamalosi o loʻo i ai uiga o le maualuga o le gaioiga ma le maualuga o le gaosiga, ma o le tulaga lelei o oloa e mautu ma faʻalagolago. I le taimi nei, ua maeʻa suʻesuʻega faʻamalosi ma atinaʻe ma faʻataʻitaʻiga, ma o le a faʻataunuʻuina le gaosiga o alamanuia.

    Tuuina atu le faʻauluina faʻamalosi ma le amataina o auaunaga faʻapitoa.

    Tala'aga o oloa

    2013—————————————Amata ma manuia le R&D

    I le amataga o le 2023—————- toe amatalia le R&D, ua maea le faamaoniga

    I le ogatotonu o le 2023———————Gaosiga faʻataʻitaʻiga faʻapisinisi

    I le faaiuga o le 2023———————Sauni mo le tilivaina

  • AOG-MAC01 benzene fa'amautu fa'ama'i fa'ama'i ile Maleic Anhydride catalyst

    AOG-MAC01 benzene fa'amautu fa'ama'i fa'ama'i ile Maleic Anhydride catalyst

    AOG-MAC01benzene fa'amautu fa'ama'i fa'ama'i ile Maleic Anhydride catalyst
    Fa'amatalaga o oloa:
    AOG-MAC01benzene fa'amautu Fa'ama'i i Maleic Anhydride catalyst taking
    Fa'afefiloi le oxide i totonu o le inert carrier, V2O5 ma MoO3e pei o vaega galue, fa'aaogaina
    I totonu o le moega fa'ama'i fa'ama'i fa'ama'iina i le maleic anhydride. O le catalyst e iai le
    Uiga o le gaioiga maualuga, maualuga le malosi, 98% -99% fua faatatau liua, lelei
    filifili ma oʻo atu i le 90% -95% fua. O le catalyst ua uma ona togafitia i le muai fa'agaoioia
    ma le faagasologa o le ola umi, o le taimi amata amata ua faʻaititia tele,
    O le ola tautua o le oloa e oʻo atu i le lua tausaga pe sili atu.
    Amioga fa'aletino ma kemisi:

    mea

    faasino igoa

    Fa'aaliga

    Lanu uliuli-lanu moana

    Ole tele ole mafiafia,g/ml

    0.75-0.81g/ml

    Fa'amatalaga o foliga, mm

    mama ga'o masani 7 * 4 * 4

    Lau'ele'ele, ㎡/g

    0.1

    Su'ega vaila'au

    V2O5, MoO3 ma faʻaopoopoga

    Malosi nutimomoia

    Axial10kg/vaega, radial5kg/vaega

    Fa'asinoga tulaga fa'atino:

    vevela, ℃

    Laasaga muamua 430-460℃, masani400-430℃

    Avanoa saoasaoa,h -1

    2000-2500

    Benzene fa'atonuga

    42g-48g /m³aafiaga lelei, 52g/ /m³e mafai ona fa'aoga

    Tulaga o gaioiga

    Benzene fua faatatau liua 98%-99%

    1. O le faʻaaogaina o le suauu-benzene e sili ona lelei i le faʻamalosi, aua o le thiophene ma le sulfur atoa i le benzene o le a faʻaititia ai le gaioiga faʻamalosi o le faʻaogaina, pe a uma le masini e masani ona taʻavale, e mafai ona faʻaaogaina le benzene superfine coking.
    2. I le faagasologa, o le vevela vevela e le tatau ona sili atu i le 460 ℃.
    3. O le saosaoa avanoa o le catalyst i totonu o le 2000-2500 h -1 o loʻo i ai le aafiaga sili. o le mea moni, afai e sili atu le saoasaoa o le avanoa nai lo lenei, e lelei foi le galue, talu ai o le catalyst lea e maualuga le saoasaoa o le avanoa.
    afifi ma felauaiga:
    I le taimi o le teuina ma le felauaiga, o le catalyst o se faʻamaoniga atoatoa o le susu, faʻafefe ma e le tatau ona sili atu i le 3 masina pe a tuʻu i luga o le ea. E mafai ona tatou fetuutuunai afifi e tusa ai ma le customers'requires.

  • Gamma activated alumina/Gamma Alumina Catalyst Carriers/gamma alumina bead

    Gamma activated alumina/Gamma Alumina Catalyst Carriers/gamma alumina bead

    Aitema

    Vaega

    I'uga

    Alumina Vaega

    Gamma Alumina

    Fa'asoaina o le Lapalapala

    D50

    μm

    88.71

    20μm

    %

    0.64

    40μm

    %

    9.14

    150μm

    %

    15.82

    Fuafuaga Fa'a-Kemikolo

    Al2O3

    %

    99.0

    SiO2

    %

    0.014

    Na2O

    %

    0.007

    Fe2O3

    %

    0.011

    Galuega Fa'aletino

    PETA

    m²/g

    196.04

    Pore ​​Volume

    Ml/g

    0.388

    Aveave le Pore Tele

    nm

    7.92

    To'atele Tele

    g/ml

    0.688

    Ua maua le alumina e le itiiti ifo i le 8 foliga, o α- Al2O3, θ-Al2O3, γ- Al2O3, δ- Al2O3, η- Al2O3, χ- Al2O3, κ- Al2O3 ma ρ- Al2O3, o latou uiga faʻavae macroscopic. e eseese foi. Gamma activated alumina o se tioata faʻapipiʻi vavalalata, e le mafai ona faʻafefe i le vai, ae solu i le acid ma le alkali. Gamma activated alumina o se lagolago malosi vaivai, e maualuga le liusuavai 2050 ℃, alumina gel i le hydrate fomu e mafai ona faia i totonu o le oxide ma le maualuga o le porosity ma le maualuga maualuga, o loʻo i ai suiga i vaega o le vevela lautele. I le maualuga o le vevela, ona o le dehydration ma le dehydroxylation, o le Al2O3surface e foliga mai o le faʻamaopoopoina o le okesene unsaturated (centre alkali) ma le alumini (centre acid), faʻatasi ai ma le catalytic activity. O le mea lea, alumina e mafai ona faʻaaogaina e fai ma ave, faʻamalosi ma cocatalyst.
    Gamma activated alumina e mafai ona pa'u, granules, fasi pepa po'o isi. E mafai ona matou faia e pei o lou manaoga.γ-Al2O3, na taʻua o le "alumina faʻagaoioia", o se ituaiga porous maualuga faʻasalalau mea mautu, ona o lona fausaga pore fetuutuunai, tele vaega faapitoa luga, faatinoga adsorption lelei, luga ma le lelei o le acidity. ma le mautu mafanafana lelei, microporous luga ma meatotino manaomia o le catalytic gaioiga, o lea e avea ai le sili ona faaaoga catalyst, catalyst carrier ma le chromatography feaveai i le alamanuia vailaau ma suauu, ma faia se matafaioi taua i le suauu hydrocracking, hydrogenation faamamaina, hydrogenation toefuataiga, dehydrogenation tali ma le ta'avale fa'amama fa'amama fa'agasologa.Gamma-Al2O3 fa'aaogaina lautele e avea ma fa'aulu fa'aoso ona o le fetuutuunai o lona fausaga pore ma le acidity luga. A faʻaaogaina γ- Al2O3 e avea o se vaʻavaʻa, e le gata i lea e mafai ona i ai ni aʻafiaga e faʻasalalau ma faʻamautu vaega galue, e mafai foi ona tuʻuina atu le nofoaga tutotonu o le alkali, tali faʻatasi ma vaega galue catalytic. O le fausaga o pore ma mea i luga o le catalyst e faʻalagolago i le γ-Al2O3 carrier, o lea o le a maua ai le maualuga o le faʻatinoga mo le faʻaogaina o le catalytic e ala i le puleaina o meatotino o le gamma alumina carrier.

    Gamma activated alumina e masani lava ona faia i lona pseudo-boehmite muamua e ala i le 400 ~ 600 ℃ maualuga le vevela o le vevela, o lea o le maualuga o le physicochemical properties e tele lava ina fuafuaina e lona pseudo-boehmite muamua, ae e tele auala e fai ai pseudo-boehmite, ma punaoa eseese. o le pseudo-boehmite e tau atu i le eseesega o gamma - Al2O3. Ae ui i lea, i na catalysts ma manaoga faapitoa i alumina ave, na o le faalagolago i luga o le pulea o le pseudo-boehmite precursor e faigata ona ausia, e tatau ona ave e prophase sauniuniga ma le post faagasologa tuufaatasia auala e fetuunai ai meatotino o le alumina e ausia manaoga eseese. A maualuga atu le vevela nai lo le 1000 ℃ i le faʻaaogaina, alumina e tupu pe a maeʻa suiga vaega: γ→δ→θ→α-Al2O3, faatasi ai ma i latou γ、δ、θ o loʻo faʻapipiʻiina vavalalata, o le eseesega e na o le tufatufaina atu o ion alumini i totonu. tetrahedral ma octahedral, o lea la o nei suiga vaega e le mafua ai le tele o fesuiaiga o fausaga. O le okesene i le vaega o le alafa'i e fa'apipi'i fa'ama'i fa'afaono, o vaega fa'alumini oxide o se fa'atasiga ogaoga, fa'aitiitiga tele le vaega o luga.

    Teuina:
    Aloese mai le susu, aloese mai le taʻavale, togi ma faʻateʻia mataʻutia i le taimi o felauaiga, e tatau ona saunia nofoaga e le timu.
    lE tatau ona teuina i totonu o faleteuoloa mago ma fa'avevela ina ia puipuia ai le fa'aleagaina po'o le susu.
    afifi:

    Ituaiga

    taga palasitika

    Pa'u

    Pa'u

    Super taga/Jumbo taga

    Lopa

    25kg/55lb

    25 kilokalama/55 lb

    150 kilokalama/330 ​​lb

    750kg/1650lb

    900kg/1980lb

    1000kg/2200 lb

  • Fa'agaoioia fa'apolopolo alumina gel/Polo alumina maualuga/alpha alumina polo

    Fa'agaoioia fa'apolopolo alumina gel/Polo alumina maualuga/alpha alumina polo

    Fa'agaoioia Spherical Shaped Alumina gel

    mo tui ile Air dryer
    Ole tele (g/1):690
    Tele Mesh: 98% 3-5mm (e aofia ai le 3-4mm 64% ma le 4-5mm 34%)
    O le vevela toe fa'afouina matou te fautuaina o le va o le 150 ma le 200 ℃
    Euiqlibrium gafatia mo vai vai e 21%

    Tulaga Su'ega

    HG/T3927-2007

    Mea Su'ega

    Tulaga masani /SPEC

    I'uga o Su'ega

    Ituaiga

    Olo

    Olo

    Al2O3(%

    ≥92

    92.1

    LOI(%

    ≤8.0

    7.1

    To'atele Tele(g / cm3

    ≥0.68

    0.69

    PETA(m2/g

    ≥380

    410

    Pore ​​Volume(cm3/g

    ≥0.40

    0.41

    Malosi Tu'i (N/G

    ≥130

    136

    Suavai adsorption(%

    ≥50

    53.0

    Ma'imau ile Attrition(%

    ≤0.5

    0.1

    Fua Fa'atatau(%

    ≥90

    95.0

  • Alfa alumina catalyst lagolago

    Alfa alumina catalyst lagolago

    α-Al2O3 o se mea porous, lea e masani ona faʻaaogaina mo le lagolagoina o catalysts, adsorbents, gas phase separation mea, ma isi. . O le tele o le pore o le α-Al2O3 catalyst carrier e sili atu le tele nai lo le molecular free ala, ma o le tufatufaina e tutusa, o le mea lea o le faʻafitauli faʻasalalau i totonu e mafua mai i le laʻititi laʻititi i le catalytic reaction system e mafai ona sili atu ona faʻaumatia, ma le loloto o le faʻamaʻiina. e mafai ona faaitiitia tali itu i le faagasologa mo le faamoemoe o le oxidation filifilia. Mo se faʻataʻitaʻiga, o le faʻamalosi siliva e faʻaaogaina mo le ethylene oxidation i le ethylene oxide e faʻaaogaina le α-Al2O3 e fai ma ave. E masani ona faʻaaogaina i faʻamatalaga catalytic ma le maualuga o le vevela ma le faʻasalalauga fafo.

    Fa'amatalaga o oloa

    Vaega Fa'apitoa 4-10 m²/g
    Pore ​​Volume 0.02-0.05 g/cm³
    foliga Spherical, cylindrical, mama fa'asao, ma isi
    Alefa fa'amamā ≥99%
    Na2O3 ≤0.05%
    SiO2 ≤0.01%
    Fe2O3 ≤0.01%
    O gaosiga e mafai ona faʻapipiʻiina e tusa ai ma manaʻoga faʻasino
  • Sulfur Recovery Catalyst AG-300

    Sulfur Recovery Catalyst AG-300

    LS-300 o se ituaiga o le sulfur toe faʻaleleia faʻamalosi faʻatasi ma se vaega faʻapitoa tele ma maualuga le gaioiga Claus. O ana fa'atinoga o lo'o tu i tulaga fa'ava-o-malo.

  • TiO2 Fa'avae Sulfur Recovery Catalyst LS-901

    TiO2 Fa'avae Sulfur Recovery Catalyst LS-901

    LS-901 o se ituaiga fou o TiO2 faʻavae catalyst ma faʻaopoopoga faʻapitoa mo le toe faʻaleleia o le sulfur. O ana fa'atinoga atoatoa ma fa'amatalaga fa'atekinisi ua o'o atu i le tulaga maualuga o le lalolagi, ma o lo'o i le tulaga ta'imua i pisinisi i totonu o le atunu'u.

  • AG-MS Spherical Alumina Carrier

    AG-MS Spherical Alumina Carrier

    O lenei oloa o se vaega polo paʻepaʻe, e le oona, leai se tofo, e le mafai ona solu i le vai ma le ethanol. O oloa AG-MS e maualuga le malosi, maualalo le ofuina o fua, fetuutuunai tele, pore voluma, vaega faʻapitoa i luga ole laiga, tele density ma isi uiga, e mafai ona fetuunai e tusa ai ma manaoga o faailoga uma, faʻaaogaina lautele i le adsorbent, hydrodesulfurization catalyst carrier, hydrogenation denitrification fa'apipi'i fa'apea, CO sulfur tete'e suiga fa'apipi'i fa'apea ma isi fanua.

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