C10G2300/305

Aviation gasolines containing mesitylene and isopentane
09816041 · 2017-11-14 · ·

Describe are preferred formulations for Avgas meeting the requirements for use in aircraft, including requirements established under ASTM standards and by the Federal Aviation Administration. In one embodiment, a binary mixture of 1,3,5-trimethyl benzene (mesitylene) and isopentane is used to provide a MON of at least 100, and more preferably at least 102. In other embodiments, the amounts of mesitylene and/or isopentane may be changed, and other fuel components are included. These various Avgas formulations are thereby adjusted to meet a variety of requirements as to octane rating, RVP, cold start, and other fuel characteristics.

FUEL COMPOSITION

Use of a liquid fuel composition comprising (a) a gasoline base fuel and (b) from 0.5 to 50% v/v of naphtha as a fuel for a spark ignition internal combustion engine, wherein the spark ignition internal combustion engine is comprised within the powertrain of a hybrid electric vehicle.

Process and system for catalytic conversion of aromatic complex bottoms

Processes and systems are disclosed for improving the yield from reforming processes. Aromatic complex bottoms, or a heavy fraction thereof, are subjected to catalytic conversion to produce additional gasoline and higher-quality aromatic compounds.

Method of reducing octane loss in catalytic cracking of gasoline in S-zorb plant
20220235279 · 2022-07-28 ·

The present invention discloses a method of reducing octane loss in catalytic cracking of gasoline in S-Zorb plant. The method comprises following steps: a. Collecting equipment data and adjusting differences thereamong to construct initial data sample set; b. Collating data sample set; c. Employing local linear s embedding to reduce dimension of independent variables, and trimming the independent variables to obtain reserved independent variables; d. Calculating correlation coefficients of the reserved independent variables and removing variables with too high correlation coefficients to obtain main variables; e. Constructing a BP neural network model of the main variables to obtain optimal octane loss prediction model; f. Employing the optimal octane loss prediction model to obtain a predicted optimal operating condition for each main variable. The present invention is different from traditional chemical mechanism method at aspect of building FCC technology process. For enterprises, they can employ it to analyze influencing factors of octane loss according to local conditions, and being able to reduce octane loss and improve quality of refined oil.

PRODUCTION METHOD OF SPARK-IGNITION ENGINE FUEL

A production method of spark-ignition engine fuel, configured to produce fuel for a spark-ignition engine, includes: mixing a light naphtha with a cyclopentane.

LIQUID-SOLID AXIAL MOVING BED REACTION AND REGENERATION DEVICE, AND SOLID ACID ALKYLATION METHOD

A liquid-solid axial moving bed reaction and regeneration apparatus and a solid acid alkylation process by using the liquid-solid axial moving bed reaction and regeneration apparatus. the liquid-solid axial moving bed reaction and regeneration apparatus comprise:

An axial moving bed reactor (1), a spent catalyst receiver (5), a catalyst regenerator (4) and a regenerated catalyst receiver (6) that are successively connected, wherein, a catalyst outlet of the regenerated catalyst receiver (6) is communicated with a catalyst inlet of the axial moving bed reactor (1);

Wherein, the axial moving bed reactor (1) is provided with at least two catalyst beds (3) arranged up and down, the axial moving bed reactor (1) is provided with a feed inlet (2) above each catalyst bed (3);

A catalyst delivery pipe (16) is arranged between two adjacent catalyst beds (3) so that the catalyst can move from top to bottom in the axial moving bed reactor (1);

A separation component (10) is provided between two adjacent catalyst beds (3), the inside space of the separation component (10) is communicated with the catalyst delivery pipe (16), the separation component (10) is for separating the stream after the reaction in the upstream catalyst bed from the catalyst, the catalyst obtained by the separation with the separation component (10) moves down through the catalyst delivery pipe (16).

PROCESS FOR PRODUCING A RENEWABLE ISOPARAFFIN COMPOUND, RENEWABLE ISOPARAFFIN COMPOUND AND USE OF THE RENEWABLE ISOPRAFFIN COMPOUND

The present invention refers to a process for producing a renewable isoparaffin compound with a high octane rating, comprising a step of Guerbet reaction between an initial C5 alcohol charge obtained from renewable raw material and methanol to produce a branched renewable C6 alcohol; dewatering of the branched renewable C6 alcohol into a C6 olefin; and hydrogenation of the C6 olefin into renewable isoparaffin. A renewable isoparaffin compound with a high octane rating, comprising at least 50% carbon of renewable natural origin in its composition, and use of said renewable paraffin in gasolines in general and in special high-performance gasolines, such as aviation gasoline, are also described.

Conversion of light naphtha to enhanced value products in an integrated two-zone reactor process

An integrated process for conversion of a hydrocarbon stream comprising light naphtha to enhanced value products. The process includes passing the hydrocarbon stream through a first reactor, the first reactor being a catalytic bed reactor with a dual-function catalyst to simultaneously reform light naphtha to BTEX and crack light naphtha to ethane, propane, and butanes. Further, the process includes passing an effluent of the first reactor to a gas-liquid separating unit to generate a liquid stream and a gas stream, and passing the gas stream to a gas separator unit to remove hydrogen gas and methane and generate an enhanced gas stream. The process further includes passing the enhanced gas stream through a second reactor, the second reactor being a pyrolysis unit operated at steam cracking conditions to convert ethane, propane, and butanes in the enhanced gas stream to light. An associated system for performing the process is also provided wherein the integrated process does not include passage of a process stream to a separate and independent hydrocracking unit to crack light alkanes in the hydrocarbon stream to smaller alkanes.

Process configuration for production of petrochemical feed-stocks

The invention relates to a process configuration for production of light olefins and aromatics from residual hydrocarbon streams. In this configuration a high severity catalytic cracking process is employed for producing higher yields of lighter olefins and various boiling fractions. C4 stream separated from gaseous product is subjected to metathesis and aromatized to form mono aromatics.

MULTI-METALLIC CATALYST DOPED WITH PHOSPHORUS AND YTTRIUM
20220168713 · 2022-06-02 · ·

The invention relates to a catalyst comprising a support, at least one noble metal M, tin, phosphorus and yttrium, the content of phosphorus element being less than or equal to 1% by weight, and the content of yttrium being less than or equal to 1% by weight relative to the mass of the catalyst. The invention also relates to the process for preparing the catalyst and to the use thereof in reforming.