Kākoʻo
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Haʻahaʻa wela hoʻololi catalyst
Catalyst hoʻololi wela haʻahaʻa:
Palapala noi
Hoʻohana ʻia ʻo CB-5a me CB-10 no ka hoʻololi ʻana i ka synthesis a me nā kaʻina hana hydrogen
Ke hoʻohana nei i ka lanahu, naphtha, ke kinoea maoli a me ke kinoea kahua aila ma ke ʻano he meaʻai, ʻoi aku hoʻi no nā mea hoʻololi haʻahaʻa haʻahaʻa haʻahaʻa axial-radial..
Nā hiʻohiʻona
Loaʻa i ka catalyst nā mea maikaʻi o ka hana ma ka wela haʻahaʻa.
ʻO ka haʻahaʻa haʻahaʻa haʻahaʻa, ʻoi aku ka nui o ke keleawe a me ka Zinc a me ka ikaika michanical maikaʻi.
ʻAno kino a me kemika
ʻAno
CB-5
CB-5
CB-10
Ka nana aku
ʻO nā papa ʻeleʻele cylindrical
Anawaena
5mm
5mm
5mm
Ka lōʻihi
5mm
2.5mm
5mm
ʻAno nui
1.2-1.4kg/l
Ka ikaika radialcrushing
≥160N/cm
≥130 N/cm
≥160N/cm
CuO
40±2%
ZnO
43±2%
Kūlana hana
Mahana
180-260°C
Paʻi
≤5.0MPa
Ka wikiwiki o ka lewa
≤3000h-1
ʻO ka ratio mokuahi
≥0.35
Komo H2Scontent
≤0.5ppmv
Komo Cl-1maʻiʻo
≤0.1ppmv
ʻO ZnO desulfurization Catalyst me ke kūlana kiʻekiʻe a me ke kumukūʻai hoʻokūkū
Ua pili ka HL-306 i ka desulfurization o ke koena o ke kinoea pohā a i ʻole syngas a me ka hoʻomaʻemaʻe ʻana i nā kinoea hānai no
nā kaʻina hana synthesis. He kūpono ia no ka hoʻohana wela kiʻekiʻe (350–408°C) a me lalo (150–210°c).
Hiki iā ia ke hoʻololi i ka sulfur organik maʻalahi i ka wā e komo ana i ka sulfur inorganic i ke kahawai kinoea. Manaʻo nui o ka
ʻO ke kaʻina hana desulfurization penei:
(1) Ka pane o ka zinc oxide me ka hydrogen sulfide H2S+ZnO=ZnS+H2O
(2) ʻO ka pane ʻana o ka zinc oxide me kekahi mau pūhui sulfur maʻalahi ma nā ʻano ʻelua.
2. Na Waiwai Kino
Ka nana aku extrudates keʻokeʻo a ʻulaʻula paha Ka nui o ka ʻāpana , mm Φ4×4–15 ʻAno nui, kg/L 1.0-1.3 3.Quality Standard
ka ikaika ʻohi, N/cm ≥50 poho ma ka attrition, % ≤6 Hiki i ka sulfur ka nui, wt% ≥28(350°C)≥15(220°C)≥10(200°C) 4. Kūlana hana maʻamau
Feedstock: kinoea synthesis, kinoea kahua aila, kinoea maoli, kinoea lanahu. Hiki iā ia ke mālama i ke kahawai kinoea me ka sulfur inorganic i ke kiʻekiʻe
e like me 23g/m3 me ka pae hoʻomaʻemaʻe ʻoluʻolu. Hiki iā ia ke hoʻomaʻemaʻe i ke kahe kinoea a hiki i ka 20mg/m3 o ia mea maʻalahi
sulfur organik e like me COS a emi iho ma mua o 0.1ppm.
5. Hoʻouka
Ke hoʻouka ʻana i ka hohonu: ʻoi aku ka L/D kiʻekiʻe (min3). Hiki ke hoʻonui i ka hoʻohana ʻana i ka hoʻonohonoho ʻana o nā reactor ʻelua
pono o ka adsorbent.
Kaʻina hoʻouka:
(1) E hoʻomaʻemaʻe i ka reactor ma mua o ka hoʻouka ʻana;
(2) E hoʻokomo i ʻelua mau kīwī kuhili me ka liʻiliʻi liʻiliʻi ma mua o ka adsorbent;
(3) E hoʻouka i kahi papa 100mm o Φ10—20mm mau pōʻai refractory ma luna o nā pahu kuhili;
(4) E nānā i ka adsorbent e wehe i ka lepo;
(5) E hoʻohana i ka mea hana kūikawā e hōʻoia i ka hāʻawi like ʻana o ka adsorbent ma kahi moe;
(6) E nānā i ke kūlike o ka moena i ka wā e hoʻouka ai. Ke makemake ʻia ka hana o loko-reactor, pono e kau ʻia kahi pā lāʻau ma luna o ka adsorbent no ka mea e kū ai.
(7) E hoʻouka i kahi mākia kuhili ʻole me ka liʻiliʻi liʻiliʻi ma mua o ka adsorbent a me kahi papa 100mm o Φ20-30mm refractory spheres ma luna o ka moena adsorbent i mea e pale ai i ke komo ʻana o ka adsorbent a hōʻoia
ka puunaue like o ke kahawai kinoea.
6. Hoʻomaka
(1) E hoʻololi i ka ʻōnaehana me ka nitrogen a i ʻole nā kinoea inert ʻē aʻe a hiki i ka emi ʻana o ka oxygen i loko o ke kinoea ma lalo o 0.5%;
(2) E hoʻomaʻamaʻa mua i ke kahawai hānai me ka nitrogen a i ʻole ke kinoea hānai ma lalo o ke kaomi a i ʻole ke kiʻekiʻe;
(3) Ka wikiwiki wela: 50 ° C / h mai ka lumi wela a hiki i 150 ° C (me ka nitrogen); 150°C no 2 mau hola (i ka wā e hoʻomehana ʻia ai
hoʻololi ʻia e hānai kinoea), 30°C/h ma luna o 150°C a hiki i ka loaʻa ʻana o ka mahana i makemake ʻia.
(4) Hoʻoponopono i ke kaomi a hiki i ka loaʻa ʻana o ke kaomi hana.
(5) Ma hope o ka hoʻomehana ʻana a me ka piʻi ʻana o ke kaomi, pono e hana mua ʻia ka ʻōnaehana ma ka hapalua o ka ukana no 8h. A laila e hoʻokiʻekiʻe i ka
hoʻouka paʻa i ka wā e paʻa ai ka hana a hiki i ka hana piha.
7. Paʻa i lalo
(1) Hāʻawi i ke kinoea (ʻaila).
E pani i nā kiwi puka komo. E mālama i ka mahana a me ke kaomi. Inā pono, e hoʻohana i ka nitrogen a i ʻole hydrogen-nitrogen
kinoea no ka mālama ʻana i ke kaomi no ka pale ʻana i ke kaomi ʻino.
(2) Hoʻololi hou o ka desulfurization adsorbent
E pani i nā kiwi puka komo. E hoʻohaʻahaʻa i ka mahana a me ke kaomi i ke kūlana ambient. A laila hoʻokaʻawale i ka
desulfurization reactor mai ka ʻōnaehana hana. E hoʻololi i ka reactor me ka ea a hiki i ka loaʻa ʻana o ka ʻike o ka oxygen o >20%. E wehe i ka reactor a wehe i ka adsorbent.
(3) Ka mālama ʻana i nā mea hana (hoʻoponopono)
E nānā i ke kaʻina hana like e like me ka mea i hōʻike ʻia ma luna koe wale nō ka hoʻohaʻahaʻa ʻana i ke kaomi ma 0.5MPa/10min a me ka mahana.
hoʻohaʻahaʻa maoli ʻia.
E mālama ʻia ka adsorbent i hoʻokuʻu ʻia i loko o nā papa ʻokoʻa. E noʻonoʻo i nā laʻana i lawe ʻia mai kēlā me kēia papa e hoʻoholo ai
kūlana a me ke ola lawelawe o ka adsorbent.
8.Ka lawe ʻana a me ka mālama ʻana
(1) Hoʻopili ʻia ka huahana adsorbent i loko o ka plastic a i ʻole ka hao hao me ka ʻili palaki e pale ai i ka makū a me ke kemika.
haumia.
(2) Pono e pale ʻia ka hāʻule ʻana, ka hui ʻana a me ka haʻalulu ikaika i ka wā o ka lawe ʻana i mea e pale ai i ka pulverization o ka
adsorbent.
(3) Pono e pale ʻia ka huahana adsorbent mai ka hoʻopili ʻana me nā kemika i ka wā o ka lawe ʻana a me ka mālama ʻana.
(4) Hiki ke mālama ʻia ka huahana no 3-5 mau makahiki me ka ʻole o ka hōʻino ʻana o kāna mau waiwai inā hoʻopaʻa pono ʻia.
No ka ʻike hou aku e pili ana i kā mākou huahana, e ʻoluʻolu e hoʻokaʻaʻike mai iaʻu.
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Nickel Catalyst E like me ka Ammonia Decomposition Catalyst
Nickel Catalyst E like me ka Ammonia Decomposition Catalyst
ʻO ka mea hoʻoheheʻe Ammonia he ʻano sec. ka mea hoʻoheheʻe hopena, e pili ana i ka nickel ma ke ʻano he mea hana me ka alumina ka mea lawe nui. Hoʻohana nui ʻia i ka mea kanu ammonia o ka mea hoʻoponopono lua o ka hydrocarbon a me ka decomposition amonia
me ka hoʻohana ʻana i ka hydrocarbon kinoea ma ke ʻano he mea maka. He kūpaʻa maikaʻi, hana maikaʻi, a me ka ikaika kiʻekiʻe.
Noi:
Hoʻohana nui ʻia ia i ka mea kanu ammonia o ka mea hoʻoponopono lua o ka hydrocarbon a me ka ammonia decomposition device,
ka hoʻohana ʻana i ke kinoea hydrocarbon ma ke ʻano he mea maka.
1. Na Waiwai Kino
Ka nana aku Slate gray raschig apo Ka nui o ka ʻāpana, mmDiameter x Kiʻekiʻe x Mānoanoa 19x19x10 ʻO ka ikaika ʻokiʻoki, N/partic Min.400 ʻOi aku ka nui, kg/L 1.10 – 1.20 Nalo ma ka attrition, wt% Max.20 ʻO ka hana catalytic 0.05NL CH4/h/g mea hoʻoheheʻe 2. Hoʻohui Kimia:
Maʻiʻo Nickel (Ni), % Min.14.0 SiO2, % Max.0.20 Al2O3, % 55 CaO, % 10 Fe2O3, % Max.0.35 K2O+Na2O, % Max.0.30 Pale wela:ʻO ka hana lōʻihi ma lalo o 1200 ° C, hoʻoheheʻe ʻole, ʻaʻole hōʻemi, ʻaʻole deformation, kūpaʻa maikaʻi a me ka ikaika kiʻekiʻe.
Ka pākēneka o nā ʻāpana haʻahaʻa haʻahaʻa (ka pākēneka o lalo o 180N/particle): max.5.0%
Hōʻailona pale wela: non-adhesion a haʻihaʻi i loko o ʻelua mau hola ma 1300°C
3. Kūlana hana
Nā kūlana hana Pumi, MPa Ka wela, °C Ka wikiwiki o ka lewa Ammonia, hr-1 0.01 -0.10 750-850 350-500 ʻAmona decomposition rate 99.99% (min) 4. Ke ola lawelawe: 2 makahiki
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High quality wholesale catalyst no ka hana hydrogenation
ʻO ka hoʻoheheʻe ʻana i ka ʻenehana
Me ka alumina e like me ka mea lawe, nickel e like me ka hana nui, ka catalyst ua hoʻohana nui ʻia i ka aila lele i ka hydrogenation dearomatization, benzene hydrogenation i cyclohexane, phenol hydrogenation i cyclohexanol hydrotreating, hydrofining o ka ʻenehana crude hexane, a me ka hydrogenation organik o unsaturated aliphatic hydro-carbons a hydrocarbons aromatic, e like me ka aila keʻokeʻo, ka ʻaila hinu hydrogenation. Hiki ke hoʻohana ʻia no ka desulfurization maikaʻi o ka wai, a me ka mea pale sulfur i ka hana hoʻoponopono catalytic. ʻO ka catalyst ka ikaika kiʻekiʻe, ka hana maikaʻi loa, i ke kaʻina hoʻomaʻemaʻe hydrogenation, hiki ke hana i ka hydrocarbon aromatic a i ʻole unsaturated i lalo i ka pae ppm. ʻO ka catalyst ka mokuʻāina i hoʻopaʻa i ka mālama ʻana.
Ma ka hoʻohālikelike ʻana, ʻoi aku ka maikaʻi o ka catalyst i hoʻohana maikaʻi ʻia i nā mea kanu i loko o ka honua, ma mua o nā huahana kūloko like.
Nā waiwai kino a me kemika:'ikamu Papa kuhikuhi 'ikamu Papa kuhikuhi Ka nana aku puʻupuʻu ʻeleʻele ʻAno nui ,kg/L 0.80-0.90 Ka nui o ke kinikini, mm Φ1.8×-3-15 Ili, m2/g 80-180 Nā ʻāpana kemika NiO-Al2O3 Ka ikaika kuʻi ʻana, N/cm ≥ 50 Nā kūlana loiloi hana:
Nā Kūlana Kaʻina Pumi pūnaewele
MpaHydrogen Nitrogen space velocity hr-1 Mahana
°CPhenol space velocity
hola-1Lakiō phenol hydrogen
mol/molPumi maʻamau 1500 140 0.2 20 Papa Hana Mea hānai: phenol, ka hoʻololi ʻana o ka phenol min 96% No nā kikoʻī hou aku e pili ana i kā mākou huahana, e ʻoluʻolu e kelepona mai iaʻu.
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ʻO ka Sulfur Recovery Catalyst AG-300
ʻO LS-300 kahi ʻano o ka sulfur recovery catalyst me kahi kikoʻī nui a me ka hana Claus kiʻekiʻe. Kū kāna mau hana ma ka pae kiʻekiʻe honua.
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ʻO TiO2 Ma muli o ka Sulfur Recovery Catalyst LS-901
ʻO LS-901 kahi ʻano hou o TiO2 i hoʻokumu ʻia me nā mea hoʻohui kūikawā no ka hoʻihoʻi sulfur. Ua hōʻea kāna mau hana piha a me nā ʻenehana loea i ka pae kiʻekiʻe o ka honua, a aia ia i ke kūlana alakaʻi i ka ʻoihana home.
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AG-MS Spherical Alumi Carrier
ʻO kēia huahana he ʻāpana kinipōpō keʻokeʻo, ʻaʻohe mea ʻawaʻawa, ʻono ʻole, hiki ʻole ke hoʻoheheʻe ʻia i ka wai a me ka ethanol. ʻO nā huahana AG-MS he ikaika kiʻekiʻe, haʻahaʻa haʻahaʻa haʻahaʻa, hiki ke hoʻololi i ka nui, pore volume, kikoʻī kikoʻī kikoʻī, bulk density a me nā ʻano ʻē aʻe, hiki ke hoʻoponopono ʻia e like me nā koi o nā mea hōʻailona āpau, hoʻohana nui ʻia i ka adsorbent, hydrodesulfurization catalyst carrier, hydrogenation denitrification mea lawe hoʻoheheʻe, CO sulfur kūpaʻa hoʻololi catalyst lawe a me nā māla ʻē aʻe.
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ʻO AG-TS Nā Microspheres alumina hoʻoikaika
ʻO kēia huahana he ʻāpana pōlele micro keʻokeʻo, ʻaʻohe mea ʻawaʻawa, ʻono ʻole, ʻaʻole hiki ke hoʻoheheʻe ʻia i ka wai a me ka ethanol. Hōʻike ʻia ke kākoʻo catalyst AG-TS e ka sphericity maikaʻi, haʻahaʻa haʻahaʻa haʻahaʻa a me ka hāʻawi like ʻana i ka nui o nā ʻāpana. Hiki ke hoʻololi ʻia ka puʻunaue nui o ka ʻāpana, ka nui o ka pore a me ka ʻili kikoʻī e like me ka mea e pono ai. He kūpono ia no ka hoʻohana ʻana ma ke ʻano he mea lawe C3 a me C4 dehydrogenation catalyst.
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AG-BT Cylindrical Alumi Carrier
ʻO kēia huahana he mea lawe alumina cylindrical keʻokeʻo, non-toxic, tasteless, insoluble in water and ethanol. ʻO nā huahana AG-BT he ikaika kiʻekiʻe, haʻahaʻa haʻahaʻa haʻahaʻa, hiki ke hoʻololi i ka nui, pore volume, kikoʻī kikoʻī kikoʻī, bulk density a me nā ʻano ʻē aʻe, hiki ke hoʻololi ʻia e like me nā koi o nā mea hōʻailona a pau, hoʻohana nui ʻia i ka adsorbent, hydrodesulfurization catalyst carrier, hydrogenation denitrification mea lawe hoʻoheheʻe, CO sulfur kūpaʻa hoʻololi catalyst lawe a me nā māla ʻē aʻe.
