Nov 18, 2017 - P-t2_YOZDk4kSHfx3P6_ggmIKFIV152l5Y9N7zl3POIwlBkFC56ERUaUKO6ndn-mXGw=w1200-h630-p' alt='Promax Software Cracked'. Feb 09, 2016  ProMax will run on Windows XP, Windows Server 2003, Windows Vista, Windows Server 2008, Windows 7, and Windows 8 operating systems (note, support for Windows XP is ending from Microsoft on April 8, 2014 and we will likewise end support at this time).

ProMax software is designed to give your dealership the competitive edge in a demanding market place. As a lead in the industry for the last 20 years, ProMax provides dealers groundbreaking and innovative features by integrating our award winning CRM, Desking and Compliance solution.

ProMax CRM, ProMax desking and the best automated Compliance Package on the market truly make ProMax Unlimited an all-in-one system. ProMax CRM, a powerful component of ProMax will help dealerships engage consumers with digital and traditional marketing and never let a prospect or customer slip through the cracks with the best status driven follow up system on the market today. Once the customer arrives, ProMax desking will help dealers increase profitability with industry-leading closing tools all while staying compliance with automated failsafe system.

FCC cracked naphtha is a valuable component of the gasoline pool that, when untreated, is characterized by high olefin and sulfur content. The limitation on sulfur of commercial gasoline imposed by tier 3, has pushed refiners to adapt existing technologies that remove sulfur in cracked naphtha to meet new and more stringent specifications. The simulation software ProMax® was used to model the desulfurization of a cracked naphtha to meet tier 3 specifications while minimizing octane loss caused by olefin saturation.

The full boiling range naphtha is sent to a post-treater complex comprising a naphtha splitter, a selective hydrogenation reactor to remove diolefins, a caustic treatment unit to remove light mercaptans, and a hydrotreating unit to selectively remove sulfur while avoiding substantial olefin saturation. The selective hydrogenation and hydrotreating reactors are modeled as plug flow reactors, with detailed reaction networks that include hydrogenation of olefins/dehydrogenation of paraffins, mercaptan, thiophene and benzothiophenes species desulfurization, and the recombination of olefins with H 2S to form mercaptan species.

The reactions in oxidizer reactor of the caustic treatment unit are considered to reach equilibrium between the reacting mercaptans and disulfide products. Different scenarios were simulated while varying the cut point in the naphtha splitter, solvent flowrate and caustic concentration in the caustic treatment unit, and reactor temperature, hydrogen to hydrocarbon ratio in the hydrotreater unit to study their effect on sulfur removal, hydrogen consumption, and research octane number of the product. Hp dc7800 pci serial port drivers windows 7.

Principialjnaya elektricheskaya shema zaryadnogo ustrojstva kulon 715d. Optimum conditions were selected for a maximum octane barrel of final product that meets a cracked naphtha sulfur specification between 10-30 ppm.