Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
  • B01D3/34—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping with one or more auxiliary substances
  • B01D3/40—Extractive distillation
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
  • B01D3/34—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping with one or more auxiliary substances
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C15/00—Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts
  • C07C15/40—Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts substituted by unsaturated carbon radicals
  • C07C15/42—Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts substituted by unsaturated carbon radicals monocyclic
  • C07C15/44—Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts substituted by unsaturated carbon radicals monocyclic the hydrocarbon substituent containing a carbon-to-carbon double bond
  • C07C15/46—Styrene; Ring-alkylated styrenes
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C7/00—Purification; Separation; Use of additives
  • C07C7/04—Purification; Separation; Use of additives by distillation
  • C07C7/05—Purification; Separation; Use of additives by distillation with the aid of auxiliary compounds
  • C07C7/08—Purification; Separation; Use of additives by distillation with the aid of auxiliary compounds by extractive distillation
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C7/00—Purification; Separation; Use of additives
  • C07C7/20—Use of additives, e.g. for stabilisation

Definitions

• Styrene and related vinyl aromatic compounds are the building blocks for numerous types of industrial products such as, for example, polymers and resins.
• Styrene can be produced as a commodity chemical through recovery from a hydrocarbon stream (e.g., pyrolysis gasoline) or by dehydrogenation of ethylbenzene.
• Isolation of a vinyl aromatic compound (e.g., styrene) from a pyrolysis gasoline stream is typically performed by extractive distillation, which typically necessitates exposure of the vinyl aromatic compound to elevated temperatures and/or oxygen. Both of these conditions can initiate unwanted thermal- or free radical-induced polymerization or oligomerization. Polymerization can lead to production losses and eventually result in system blockages of the apparatus being used for separating the vinyl aromatic compound from the hydrocarbon stream.
• a combination of dinitrophenolic compound and a nitroxyl free radical compound of have been used to inhibit vinyl aromatic compound polymerization.
• a combination of a 2-nitrophenolic compound in combination with a sulfonic acid compound has also been used to inhibit vinyl aromatic compound polymerization.
• the present disclosure describes methods for inhibiting polymerization of vinyl aromatic compounds during extractive distillation.
• the methods include steps of a) providing a mixture having at least one vinyl aromatic compound, b) adding at least one dinitrophenol inhibitor to the mixture, and c) after step b) occurs, performing an extractive distillation on the mixture to isolate the at least one vinyl aromatic compound.
• a single vinyl aromatic compound is isolated.
• the single vinyl aromatic compound is styrene.
• aromatic refers to aromaticity, a chemical property in which a conjugated ring of unsaturated bonds, lone pairs, or empty orbitals exhibit a stabilization stronger than would be expected by the stabilization of conjugation alone. It can also be considered a manifestation of cyclic derealization and of resonance stabilization. This is usually considered to be because electrons are free to cycle around circular arrangements of atoms, which are alternately single- and double-bonded to one another.
• aliphatic refers to compounds having carbon atoms that are capable of being joined together in straight chains, branched chains, or rings (in which case they are called alicyclic).
• polymer will collectively refer to polymers of vinyl aromatic compounds including dimers, trimers, higher oligomers and polymers.
• Embodiments of the present disclosure are generally directed toward methods for inhibiting thermal- and free radical-induced polymerization of vinyl aromatic compounds during extractive distillation processes.
• vinyl aromatic compounds may be exposed to low levels of oxygen and high temperatures (about 8O 0 C to about 16O 0 C) for varying lengths of time. These conditions are conducive toward inducing polymerization of the vinyl aromatic compounds.
• a dinitrophenol inhibitor can minimize or substantially prevent polymerization of vinyl aromatic compounds during extractive distillation processes under conditions in which polymer formation occurs within minutes in the absence of an inhibitor.
• the dinitrophenol compound is 2-sec-butyl-4,6-dinitrophenol (DNBP), which may be used alone to inhibit polymerization.
• DNBP 2-sec-butyl-4,6-dinitrophenol
• the present disclosure describes methods for inhibiting polymerization of vinyl aromatic compounds during extractive distillation.
• the methods include steps of a) providing a mixture having at least one vinyl aromatic compound, b) adding at least one dinitrophenol inhibitor to the mixture, and c) after step b) occurs, performing an extractive distillation on the mixture to isolate the at least one vinyl aromatic compound.
• the at least one aromatic compound includes styrene.
• a single vinyl aromatic compound is isolated from the extractive distillation.
• the single vinyl aromatic compound is styrene.
• the mixture also includes contaminants from which the vinyl aromatic compounds are to be separated.
• Such contaminants include, for example, aliphatic compounds, aromatic compounds, other vinyl aromatic compounds, sulfur-containing compounds, colored impurities and combinations thereof.
• styrene is presented as an illustrative vinyl aromatic compound that can be isolated according to the methods described in the present disclosure. However, one of ordinary skill in the art will recognize that other vinyl aromatic compounds may be isolated through routine experimental modifications of the embodiments described herein, such modifications residing within the spirit and scope of the present disclosure.
• styrene can be isolated from pyro lysis gasoline using methods described in United States Patents 5,849,982 and 5,877,385, each of which are incorporated by reference herein in their entirety.
• Polymer can form and accumulate, leading to system breakdown, under these conditions in the absence of an inhibitor.
• the extractive distillation is performed at a temperature of at least about 100 0 C. In other various embodiments, the extractive distillation is performed at a temperature between about 8O 0 C and about 16O 0 C.
• dinitrophenol and related nitrophenol compounds are known in the art, Applicants believe that the present disclosure is the first to demonstrate that high concentrations of these moieties can be used to inhibit polymerization upon exposure to conditions commonly encountered during extractive distillation.
• polymerization of vinyl aromatic compounds can be minimized or substantially prevented by adding a dinitrophenol or related nitrophenol inhibitor to a hydrocarbon stream before isolation of the vinyl aromatic compound from the stream.
• the dinitrophenol compound is 2-sec-buyl- 4,6-dinitrophenol (DNBP).
• DNBP 2-sec-buyl- 4,6-dinitrophenol
• the hydrocarbon stream is a pyrolysis gasoline stream.
• the polymerization that is inhibited is a thermal-induced polymerization. In other various embodiments, the polymerization that is inhibited is a free radical-induced polymerization.
• a concentration of DNBP or other dinitrophenol inhibitor in the hydrocarbon stream determines the effectiveness of inhibiting polymerization of the vinyl aromatic compound. For example, in the embodiments presented herein, adding DNBP at high concentrations may substantially prevent polymerization of the vinyl aromatic compound.
• concentrations of DNBP and other dinitrophenol inhibitors described in the embodiments presented herein are considerably higher than are commonly encountered in other applications in which polymerization of a vinyl aromatic compound is inhibited.
• a concentration of DNBP is at least about 10,000 wt. ppm with respect to the at least one vinyl aromatic compound of interest. In other various embodiments, a concentration of DNBP is between about 10,000 wt.
• a concentration of DNBP is between about 10,000 wt. ppm and about 15,000 wt. ppm. In yet additional embodiments, a concentration of DNBP is about 14,000 wt. ppm.
• Example 1 A dinitrophenol inhibited mimetic feed representing a styrene extractive distillation column bottom was prepared where 95% extractive agent was mixed with 5% styrene with and without varying doses of DNBP as shown in Table 1.

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• Chemical & Material Sciences (AREA)
• Organic Chemistry (AREA)
• Engineering & Computer Science (AREA)
• Analytical Chemistry (AREA)
• Oil, Petroleum & Natural Gas (AREA)
• Water Supply & Treatment (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

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Citations (8)

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• 2010
  • 2010-02-15 US US12/705,937 patent/US8771476B2/en not_active Expired - Fee Related
  • 2010-04-23 CN CN201010158962.1A patent/CN101955409B/zh not_active Expired - Fee Related
  • 2010-05-22 BR BR112012001138A patent/BR112012001138A2/pt not_active IP Right Cessation
  • 2010-05-22 KR KR1020127004130A patent/KR20120049270A/ko not_active Ceased
  • 2010-05-22 EP EP10800200A patent/EP2453999A4/en not_active Withdrawn
  • 2010-05-22 WO PCT/US2010/035889 patent/WO2011008343A1/en not_active Ceased
  • 2010-05-22 RU RU2012105429/04A patent/RU2531918C2/ru not_active IP Right Cessation
  • 2010-05-22 IN IN1380DEN2012 patent/IN2012DN01380A/en unknown
  • 2010-06-22 TW TW099120243A patent/TWI492933B/zh not_active IP Right Cessation

Patent Citations (8)

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