Deoxygenation Odino Dehydrogenation Catalyst

 

Say CAS-KR-T01-K Deoxygenation o Dehydrogenation catalyst et ginawa diad impangusar na activated alumina bilang suporta, nikadkaduman rare earth bilang additive material tan atagey a karga na precious metals Pd tan Pt bilang aktibon grupo, ya malaknab ya uusaren ed industriya na panaglinis na gas.

Diad inkalapagan, say gas purifying production et kaukolan ya ekalen so trace oxygen ed gas, pian naseguro so kalinisan na gas; say trace oxygen ed syngas, coal gas tan coking gas et mainomay ya pansengegan na catalyst poisoning ed ontumbok a proseso, kanian kaukolan met ya ekalen so trace oxygen, say Deoxygenation o Dehydrogenation catalyst tayo et akagawa ed saya diad deoxidation depth ya 1ppm.

Say CAS-KR-T01-K Deoxygenation o Dehydrogenation catalyst et manunan uusaren parad pangekal tan panaglinis na hydrogen ed oxygen, dagem tan atmospera ya walay oxygen to, singa legan na hydrogen tan produksyon na oxygen ed industrial water electrolysis, say oxygen et mangeekal na hydrogen, say pangekal na hydrogen gas ed kuarto na operasyon, singa say electrolysis, satellite, power station, battery room, submarine, tan arum ni tan say pangekal na hydrogen tan panaglinis na electrochemical medical oxygen generator.

CAS-KR-T01-K Deoxygenation o Dehydrogenation catalyst pictures

 

 

 

 

Anggapoy kaukolan ya pambawas tan pangipaaktibo antis ya usaren, say hydrogen deoxidation tan inert gas dehydrogenation et nayarin igapo ed temperatura na kuarto, tan say oxygen et nayarin naekal ed kulang ya 1ppm (anggad 0.02ppm) no usaren ed (3~10) ×103 h-1 space speed, say deoxidization na synthetic coking, tan coking gas et nayarin igapo ed silong na coking diad kondisyon ya 110~140 degree, say presyon et mas atagey nen say 0.1MPa tan say kapeles na liwang et (1~4) ×103 h-1, say nakekeraan ya oksiheno et kulang ed 1ppm. say dehydrogenation et nayarin igapo ed temperatura na kuarto (80~120℃so sankaabigan ya temperatura na operasyon), diad silong na kondisyon na reaksion ya 10~103-13 h-13h. diad gas ya linisan et nayarin naekal ed leksab na 5ppm, say sankatageyan ya temperatura na resistensya ed petang et 650~750 degree, say biskeg na makina et maong, say bilay na serbisyo to et masulok ya 3 taon.

 

 

Say ratio na katagey/diametro na karga na catalytic reactor	Mas baleg nen say 1
Temperatura na operasyon	Normal ya temperatura~250 degree
Kapeles na liwang	Mas abeba odino mipara ed 3000 h-1
Kapasidad na deoxygenation; O2,H2Say peles na panaglinis	Mas baleg nen say 15mlO2/g; Mas baleg nen say 95%
Kaaralem na deoxygenation tan dehydrogenation	Mas abeba odino mipara ed 1.0ppm, Mas abeba odino mipara ed 50ppm
Itsura	Brown ,gray;sphere 1~6mm
Bulk density	0.68 ± 0.05g/ml
biskeg na panagmekmek	Mas baleg nen say 60N/pcs
Bilay na serbisyo	2-3 taon

 

 

Parad panaglinis na puron gas (singa say hydrogen, inert gas, nitrogen tan arum niran panaggawa na gas ya atagey so puro to), kaslakan ya uusaren tayo so hydrogen deoxygenation (say panaglinis na hydrogen et walaan na mismon hydrogen tan agto kaukolan so hydrogen); Say oxygen purification et kaukolan ya ekalen so trace hydrogen ed gas, say catalyst et tatawagen la natan ya dehydrogenation agent, mankikimey ira ed parehon prinsipyo a singa onggendan:

Bangta say syngas, gas tan coking gas et kaslakan ya manguusar na dilin hydrogen tan carbon monoxide da pian na-deoxidize.

Saray kakaukolanen ed pangusar na proseso:paulyanan so feed gas ya ondalan ed catalyst bed manlapud tagey ya anggad leksab, kontrolen so peles na dagem, tan kalkalnan pabalegen so gas flow rate, Isuheri ya mangiyan na preheater antis na dehydrogenation reactor pian onggapo. no onggapo, no kaukolan ya onggapo panamegley na panagpainit, sarag mon isara so preheater kayari na mapatnag ya intagey na temperatura na catalyst bed. tan nepeg ya idagdag so cooler kayari na reactor pian napaway so danum ya nagawa ed reaction ed panapanaon

 

 

1) No say catalyst et seryoso lan nasepsep na danum odino nabasa ed danum, nayarin pamaraan ed 110℃ed loob na 6 oras pian nawalaan na regeneration.

2) )no say catalyst et mantsa na lye, nayarin urasan na pigaran danay na anion (singa say AC -) odino deionized water, pamaraan, pian na-regenerate, tan nepeg ya napaliisan so ammonia condensation ed catalyst.

3) No say catalyst et nadutakan na larak, nayarin napasimbalo itan na oxygen- ya walay gas (odino dagem) to ed 500~550℃ed loob na 3~5 oras, insan nabawasan na H2 ed 200℃ed loob na 2~4 oras pian napasimbalo itan.

4) No say catalyst et na-deactivate lapud sulfide poisoning, nayarin i-regenerate panamegley na dagem ed loob na 4~8 oras ed 300~500℃insan nabawasan na H2300~500℃ed loob na 4 oras pian na-regenerate.

 

 

Say deoxidizer (hydrogen) agent et manunan uusaren parad panaglinis na gas, panaglinis tan arum niran managgaway gas.

Say deoxidizer et nayarin usaren met ed synthetic gas, gas, coke gas refining workshop na synthetic ammonia tan arum niran industriya na kemikal; nausar met ed industriya na float glass, color TV tan sistema na panaglinis na gas ya linya na produksyon na industriya na elektroniko; uusaren met ed saray olefins deoxygenation refining, petrochemical polyethylene, polypropylene production tan arum nira. say oxygen content ed gas et kaukolan ya abeba nen 0.1 PPM (Lapud say trace amount na 02 et onreak ed catalyst tan mamawala na aktibidad na synthetic olefin catalyst, tan diad saman met a panaon et onreak ed saray substansia ed reaction system pian manporma na resin, ya mangamper ed saray pores tan pipes na synthetic catalyst).

 

 

 

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