Classifications

• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C41/00—Preparation of ethers; Preparation of compounds having groups, groups or groups
  • C07C41/01—Preparation of ethers
  • C07C41/05—Preparation of ethers by addition of compounds to unsaturated compounds
  • C07C41/06—Preparation of ethers by addition of compounds to unsaturated compounds by addition of organic compounds only

Definitions

• the present invention relates to a process for the r preparation of a Ik L-te rt-buty L ethers in the presence of butadi ene .
• Suitable olefinic fractions for said syntheses are the C. cuts outcoming from catalytic cracking, or those t*
• the feed olef nic charges the C. fractions from catalyt c cracking, or those deriving from steam cracking after butadiene removal are used, and as the
• mt content charge (containing from 10 to 70% by weight of butadiene), such as the C. cut before butadiene extraction, the operating conditions have to be exactly defined to the purpose of recovering more than 98-99% of
• a certain amount of dissolved oxygen can be occasionally present also in the liquified C, fraction
• the procedures for oxygen removal are those known in the art for the removal of inert gases dissolved in liquid products, such as, e.g., the use of a suitable stripper, consisting in a distillation column, from the bottom of which the oxygen-free product is obtained, whilst oxygen is discharged as a overhead vent from the reflux accumulator.
• the process of the present invention is a process for the preparation of alkyl-tert-but l ethers by starting from C. charges containing isobutene and
• H a other C. hydrocarbons, among which butadiene at a concentration, referred to the total charge, comprised within the range of from 10% by weight to 70 by weight (C charges coming from catalytic cracking or from steam cracking without butadiene removal) and from aliphatic alcohols preferably selected from methanol and ethanol
• a d comprises reacting the isobutene contained in the charge with the aliphatic alcohol in one or more reaction sections at a temperature not higher than 60 C in the presence of a macroporous sulphonated resin of Amberlyst 15 or Lewatit SPC 108 type and separating the alkyl-tert- butyl ether from the other unreacted components by dist llation, and is characterized in that the alcohol and/or the C. hydrocarbon charge are/is submitted, before 4 the reaction, to an oxygen removal step, in particular of physical type, of removal of dissolved free oxygen by stripping by outer inert agents, or distillation up to reduce the free oxygen content to 1-2
• the oxygen removal may be carried out by stripping by a stream of a suitable inert gas, such as nitrogen, methane, hydrogen, fuel gas, ethane, etc., or mixtures thereof.
• a suitable inert gas such as nitrogen, methane, hydrogen, fuel gas, ethane, etc., or mixtures thereof.
• Figure 1 constituted by a C. cut from steam cracking
• the olefinic cut (1) has a content of dissolved oxygen Lower than 1 ppm, w ilst methanol, which is stored inside a tank under an air atmosphere, has an oxygen content ranging from 30 to 60 mg/l.
• an alcoholic solution of a polymerization inhibitor is injected (8) in such an amount that in the combined charge (3) theINDibitor concentration ranges from 60 to 120 ppm.
• the reaction product (4) containing an average amount of 30.7% of MTBE, which justifies an isobutene conversion of 90%, is fed to a fractionation tray column (9) in such an intermediate point, that the rectification section represents 40% of column.
• oxygen reaches values comprised within the range of from 3000 to 6000 ppm.
• Feed conditions and reflux are such that the pressure drop L ? , which is established in the column, is of 0.3 bars .
• A.P rises up to values more than double of the initial value, while the fractionation capacity results seriously i pai red.
• Example 1 MTBE synthesis and fractionation are carried out as in Example 1, with the difference that the polymerization inhibitor is injected, by the stream (8), Figure 1, also to the column reflux.
• Examg_e_3 MTBE synthesis and fractionation are performed under operating conditions analogous to those of Example 1, with the variant (see Figure 2) of the treatment of methanol (2),which contains an amount of dissolved oxygen ranging from 30 to 60 mg/l, and is delivered to the upper section of a stripping column (12), from the bottom of which a stream of an inert gas, such as fuel gas (13), containing an oxygen amount lower than 150 ppm, is sent in countercurrent flow.
• an inert gas such as fuel gas (13)
• the oxygen-depleted methanol, stream (15), is recovered from the bottom of the column, with oxygen levels constantly Lower than 1 ppm.
• the oxygen-enriched stripping gas (14) is sent to blowdown.
• the efficaciously of the stripping is also confirmed by the fact that in gaseous stream (7) the oxygen level does not exceed 20 ppm.
• column (9) has been operating for 8000 hours with no drawbacks, and an inspection thereof sho ed the complete absence of polymerization phenomena.
• the equal find numbers have the same meaning as of Figure 1.
• MTBE synthesis and its fractionation are carried out as in preceding Examples, but methanol is now deprived of oxygen by sending stream (2) ( Figure 3) to the head of a distillation column (12), from the bottom of which methanol is recovered with an oxygen Level lower than 0.5 ppm.
• the ini ially dissolved oxygen is removed as a overhead vent (14) from reflux accumulator (13).
• the oxygen amount found in the overhead vent (7) is lower than 10 ppm.

Landscapes

• Chemical & Material Sciences (AREA)
• Organic Chemistry (AREA)
• Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
• Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Priority Applications (7)

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Publications (1)

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Cited By (4)

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Citations (4)

• 1986
  • 1986-05-27 IT IT20575/86A patent/IT1190015B/it active
• 1987
  • 1987-05-06 IN IN328/MAS/87A patent/IN169670B/en unknown
  • 1987-05-06 IN IN327/MAS/87A patent/IN170000B/en unknown
  • 1987-05-07 BR BR8707694A patent/BR8707694A/pt unknown
  • 1987-05-07 JP JP62503293A patent/JPH01503062A/ja active Pending
  • 1987-05-07 HU HU873101A patent/HU198166B/hu not_active IP Right Cessation
  • 1987-05-07 AT AT87903295T patent/ATE71077T1/de active
  • 1987-05-07 RO RO1987135631A patent/RO101206B1/ro unknown
  • 1987-05-07 DE DE8787903295T patent/DE3775774D1/de not_active Expired - Fee Related
  • 1987-05-07 EP EP87903295A patent/EP0307404B1/en not_active Expired
  • 1987-05-07 WO PCT/EP1987/000241 patent/WO1987007259A1/en not_active Ceased
  • 1987-05-13 GR GR870749A patent/GR870749B/el unknown
  • 1987-05-15 CS CS354387A patent/CS273640B2/cs unknown
  • 1987-05-21 TR TR87/0345A patent/TR23863A/xx unknown
  • 1987-05-21 YU YU00912/87A patent/YU91287A/xx unknown
  • 1987-05-22 ES ES878701708A patent/ES2006492A6/es not_active Expired
  • 1987-05-25 DD DD87303103A patent/DD256862A5/de not_active IP Right Cessation
  • 1987-05-25 PL PL1987265893A patent/PL150603B1/pl unknown
  • 1987-05-27 AR AR87307671A patent/AR242768A1/es active
• 1988
  • 1988-01-27 NO NO880345A patent/NO166279C/no unknown

Patent Citations (4)

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