Catalytic distillation drives superior process efficiency by combining reaction and fractionation into a single unit operation. As an important part of our Light Molecules portfolio, this process intensification offers advanced solutions for ethers, (CDMtbe, CDEtbe, CDTame, CDTaee, CDEthers, CDDME), hydrogenation (CD Hydro), and desulfurization (CDHDS/CDHDS+). These technologies help refiners optimize production while minimizing energy consumption and plot space.
- High conversion
- High purity ethers
- Simple and effective control of reaction temperature
- Most effective heat removal technique
- Low capital and energy costs
- High conversion
- High-purity ethers
- Simple and effective control of reaction temperature
- Most effective heat removal technique
- Low capital and energy cost
- High conversion
- Simple and effective control of reaction temperature
- Most effective heat removal technique
- Low capital and energy costs
- High conversion
- Simple and effective control of reaction temperature
- Most effective heat removal technique
- Low capital and energy costs
- High conversion
- Simple and effective control of reaction temperature
- Most effective heat removal technique
- Low capital and energy costs
- High selectivity to C8 isoolefins production
- Low capital and energy costs
- Integrated Design: Combines reaction and pre-fractionation and stabilizer in a single unit operation
- Cost-Effective: Requires less equipment than traditional methods and eliminates the need for a hydrogen compressor
- High Conversion: True counter-current operation results in high single-pass conversions for benzene and hydrogen thus eliminating the hydrogen compressor
- Low Pressure operation allows all carbon steel construction
- Precise Control: Constant pressure boiling ensures exact temperature control in the catalyst zone
- Flexible: Applicable to hydrocarbon streams of both low and high benzene content
- Lower capital costs due to process intensification
- High selectivity to olefins
- Long catalyst life eliminating need for regeneration and associated equipment
- Distillate product is essentially hydrogen free
- C5 distillate is also made mercaptan sulfur free within the process
- Lower capital costs due to process intensification
- High purity products in single step operation
- Long catalyst life eliminates need for regeneration
- High selectivity and yield to olefins
- Full separation of isobutylene from n-butenes
- Preserves light olefins in the LCN cut
- The distillate product is essentially mercaptan-sulfur free
- Isomerization of alfa olefin to beta olefins further enhances octane number value
- Lower capital costs due to process intensification
- Highly selective process
- Capital and operational cost savings
- Feed processing flexibility
- Proven long-term operation worldwide
- Easier operation than fixed-bed reactors
- Essentially mercaptan-free gasoline product
- Ultra-low sulfur gasoline targeting <100 wppm in light fraction and <0.5 wppm in aromatics-rich cut
- Minimum aromatic hydrogenation (<2 wt %) while maintaining olefin content in the final blend
- Efficient hydrogen usage
- Achieves >99.9 wt % conversion of diolefins
- Near-equilibrium conversion of the contained isobutene per pass is achieved at greater than 85% selectivity to isobutene and isopentene
- Hydrocarbon feed containing linear C4 and C5 olefins such as FCC and Steam cracker C4 andC5 cuts can be processed without steam or other diluents, and without the addition of catalyst activation agents to promote the reaction
- High yield of isobutene and isopentenes
- The isomerate product is suitable for making various petrochemicals, such as MTBE, ETBE TAME or HPIB
- Combined with our ethers or the CDHydro Deisobutenizer technology it can achieve high conversion
- Near-equilibrium conversion of the contained isobutene per pass is achieved at greater than 85% selectivity to linear-butenes
- Hydrocarbon feed containing isobutene, such as C4 raffinate or FCC C4s, can be processed without steam or other diluents, and without the addition of catalyst activation agents to promote the reaction
- High yield of n-butenes
- The butene isomerate is suitable for making various petrochemicals, such as propylene via Olefin Conversion Technology
- Combined with the CDHydro Deisobutenizer technology, it can achieve high conversion
- Optimizes performance and lowers capital and operating costs
- Novel reaction system featuring a unique design that improves mass transfer
- Feedstock flexibility. Capable of processing both C4 and C5 olefin streams
- Superior product purity. Improved Alkylate quality: higher ROAD and lower sulfur concentration
- Economic efficiency. Proven, profitable method for producing premium fuel with minimum acid consumption
- Elimination of post treatment for the reaction product (Acid, Caustic and Water washing for the reaction product is eliminated)
- Improves operational reliability
- True solid catalyst alkylation process
- Eliminates the need for acid mitigation systems
- Simplifies revamps, using existing infrastructure
- High MTBE or ETBE conversion
- High Isobutylene yield
- Low by-product formation
- Low overall capital and energy costs
- High C8 isoolefins selectivity and yield
- Low by-product formation
- Low overall capital and energy costs
Meeting the demand for cleaner energy requires efficient routes to produce low-carbon, drop-in fuels. Our portfolio addresses this challenge with advanced processes for bio-ethers production such as bio-MTBE, bio-ETBE, bio-TAME, bio-TAEE and rDME and Ethanol to Alkylate. By bridging the gap between renewable feedstocks and high-performance fuel specifications, these solutions help producers reduce carbon intensity without compromising operational reliability.
- World’s first renewable alkylate
- World-scale production capability
- Commercially demonstrated ethanol dehydration to ethylene technology
- Three large-scale Ethylene Dimerization units in operation (more than 37 years of commercial experience)
- More than ten years of commercialization for the Lummus EtJ oligomerization catalyst
- More than 30 years of experience in the hydroprocessing of hydrocarbons
- Synergetic integration of the Ethanol Dehydration, Dimerization, Oligomerization, and Hydrogenation steps for optimal yield and high selectivity to SAF components
