Catalytic processing, gasoline

Toluene disproportionation (TDP) is a catalytic process in which 2 moles of toluene are converted to 1 mole of xylene and 1 mole of benzene this process is discussed in greater detail herein. Although the mixed xylenes from TDP are generally more cosdy to produce than those from catalytic reformate or pyrolysis gasoline, thek principal advantage is that they are very pure and contain essentially no EB. 

Ethers, such as MTBE and methyl / fZ-amyl ether (TAME) are made by a catalytic process from methanol (qv) and the corresponding isomeric olefin. These ethers have excellent octane values and compete on an economic basis with alkylation for inclusion in gasoline. Another ether, ethyl tert-huty ether (ETBE) is made from ethanol (qv) and isobutylene (see Butylenes). The cost and economic driving forces to use ETBE vs MTBE or TAME ate a function of the raw material costs and any tax incentives that may be provided because of the ethanol that is used to produce it. 

Hydrocarbons from Synthesis Gas and Methanol. Two very important catalytic processes in which hydrocarbons are formed from synthesis gas are the Sasol Eischer-Tropsch process, in which carbon monoxide and hydrogen obtained from coal gasification are converted to gasoline and other products over an iron catalyst, and the Mobil MTG process, which converts methanol to gasoline range hydrocarbons using ZSM-5-type 2eohte catalysts. 

Through the 19.30s, Ipatieff led UOP in its effort to develop two catalytic processes for the production of high-octane fuel alkylation and polymerization— the first, a reaction of a hydrocarbon with an olefin (double-bonded compound) the second, the formation of long molecules from smaller ones. Both processes produce high-octane blending compounds that increase the quality of cracked gasoline. 

MBR [Mobil benzene reduction] A catalytic process for reducing the benzene content of gasoline. It combines features of three earlier processes benzene alkylation with tight olefins, olefin equilibration with aromatization, and selective paraffin cracking. The olefins are obtained from FCC offgas. The catalyst is a modified ZSM-5 zeolite. Developed by Mobil Research Development Corporation in 1993. 

NExTAME [Neste tertiary amyl methyl ether] A catalytic process for converting C5, C6, and C7 tertiary olefins to ethers for blending into gasoline to increase its octane rating. Developed by Neste Oy in 1994 and commercialized at Porvoo, Finland, in 1995. 

SULFREX A catalytic process for removing sulfur compounds from LPG, gasoline, and kerosene. Developed by Total/IFP in the 1980s and operated in Tenguiz, CIS, since 1991. 

The contribution from Catalysis to the economics is remarkable. Based on estimates from the North American Chemical Society between 15 and 20%f the world gross net product are provided by catalytic processes [5]. Thereby the catalysis costs are much less than the sales revenues from the products, which they help to create, making catalysis a key technology to the sustainable and cost effective production of chemicals. Numerous things of our daily life like gasoline, plastics, cars, computers or drugs would not exist at all or at least not be available in the today s quality without catalysis. At BASF for example over 80%f the 8000 products see at least once a catalyst during their production cycle. 

The isoprene monomer is not readily available from direct cracking processes. Several routes are employed for its synthesis. One route begins with the extraction of isoamylene fractions from catalytically cracked gasoline streams. Isoprene is produced by subsequent catalytic dehydrogenation. 

Crude oil typically contains little to no olefinic compounds. Through refining and processing, however, olefins are produced and become a part of various crude oil fractions. Olefins can be found in thermally cracked and catalytically cracked gasoline fractions as well as in FCC cycle oils and coker gas oils. For this reason, it is not unusual for finished gasoline and distillate blends to contain a high-olefin-content stream. 

Reforming Both thermal and catalytic processes are utilized to convert naphtha fractions into high-octane aromatic compounds. Thermal reforming is utilized to convert heavy naphthas into gasoline-quality aromatics. Catalytic reforming is utilized to convert straight-run naphtha fractions into aromatics. Catalysts utilized include oxides of aluminum, chromium, cobalt, and molybdenum as well as platinum-based catalysts. 

The application of catalysis to the production of motor fuel by cracking of less volatile petroleum oils was first investigated in France by Eugene J. Houdry in the period 1927 to 1930. The results from these investigations clearly established the superiority of catalytically cracked gasoline over that made by the thermal processes the economic possibilities were also indicated. 

In broad terms, alkylation refers to any process, thermal or catalytic, whereby an alkyl radical is added to a compound. In the petroleum industry, however, the term alkylation generally refers to the catalytic process for alkylating isobutane with various light olefins to produce highly branched paraffins boiling in the gasoline range. This specific process will be discussed in this paper. 

From 1943 to 1948 he was consultant to Hydrocarbon Research, Inc., and from 1948 until his death a consultant to the Socony-Vacuum laboratories in connection with the synthesis of gasoline and the cracking and re-forming of petroleum by catalytic processes. 

---