Follow us :

Hydrogenation Catalyst with Stable Structure for Purification Process

Hydrogenation Catalyst with Stable Structure for Purification Process
Hydrogenation Catalyst with Stable Structure for Purification ProcessHydrogenation Catalyst with Stable Structure for Purification ProcessHydrogenation Catalyst with Stable Structure for Purification ProcessHydrogenation Catalyst with Stable Structure for Purification Process
group name
Hydrodesufurization Catalyst
Min Order
1 ton
brand name
Syamcat Catalyst Manufacturer
model
SYAMCAT YJ17/SYAMCAT YJ18/SYAMCAT YJ19
Nearest port for product export
qingdao
Delivery clauses under the trade mode
FOB, CFR, CIF, EXW, FCA
Acceptable payment methods
T/T, L/C
update time
Fri, 30 Oct 2026 00:30:19 GMT

Paramtents

  • Active Components Cobalt Molybdenum Nickel

  • Catalyst Carrier Alumina-Titania

  • Color Gray-green

  • Crushing strength/(N.cm-1) ≥150

Packging & Delivery

  • Min Order1 ton

Briefing

YJ17/YJ18/YJ19 in the methanol plant range. Discuss feedstock treatment requirements before reforming.

Detailed

YJ17/YJ18/YJ19 Hydrogenation Catalysts — Methanol Plant Feed Review

SYAMCAT YJ17, YJ18 and YJ19 are hydrogenation catalyst grades with cobalt, molybdenum and nickel active components. This page presents the grades within the methanol plant feed purification range.

For a methanol plant enquiry, please identify the feedstock, hydrogen availability, organic sulfur and olefin content, upstream treatment and the downstream reforming process. Review hydrogenation and subsequent desulfurization requirements together.

SYAMCAT Hydrogenation Catalyst

Operating Conditions

Item
SYAMCAT YJ17
SYAMCAT YJ18
SYAMCAT YJ19
Temperature/℃

450-650

450-650

450-650

Pressure/MPa
Atmospheric-6.0
Atmospheric-6.0
Atmospheric-6.0
Olefin Content, %
≥2.7
≥2.7
≥2.5
Organic sulfur content/ppm
500-2000

500-2000

500-2000

Space velocity/h-1
≤3000
500-3000
500-3000

Specifications

Item
SYAMCAT YJ17
SYAMCAT YJ18
SYAMCAT YJ19
Shape
Spheres
Extrudate
Extrudate
Size/mm
φ3.5-5.5
φ2-3
φ2-3
Active component
Co-Mo-Ni
Co-Mo-Ni
Co-Mo-Ni
Bulk density/(kg.L-1)
0.70-0.90
0.45-0.65
0.45-0.65

Selection and Loading Considerations

Feed Hydrogenation

Review organic sulfur conversion and olefin saturation requirements against the actual feed and available hydrogen.

Reactor Configuration

Provide reactor dimensions, bed arrangement and current catalyst loading so that grade selection can be reviewed.

Startup and Operating Instructions

Confirm the current grade-specific technical data sheet and startup procedure before setting operating conditions.

Discuss Your Methanol Plants Requirements

Please share the feed composition, sulfur species and concentrations, olefin content where applicable, gas flow, operating conditions, vessel dimensions, current catalyst or sorbent loading and the required outlet specification.

Discuss Catalyst Selection