Purification process for preparing C4 materials for isobutene by C4 linear chain olefin skeleton isomerism

A technology for purifying processes and materials, which is applied in the petrochemical field and can solve problems such as poor selectivity, poisoning and deactivation of heterogeneous catalysts

Inactive Publication Date: 2010-09-15
CHINA UNIV OF PETROLEUM (BEIJING)
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The existence of propylene, isobutylene, C5 and components above C5 in the C4 raw material will easily deactivate the coke of the heterogeneous catalyst, and the above components will polymerize or crack carbon deposits on the catalyst; Deactivation, so it must be removed before isomerization; sulfur is easily adsorbed on the active center of the isomerization catalyst, causing partial poisoning of the isomerization catalyst, and sulfur is also easy to deactivate the butadiene (BD) hydrogenation catalyst, so the material is required The total sulfur in the medium is less than 1ppm; organic oxides include organic alcohols, ketones, acids, esters, ethers, etc., such as methanol, dimethyl ether, methyl ethyl ketone, tert-butanol, etc., which are easy to poison the...

Method used

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  • Purification process for preparing C4 materials for isobutene by C4 linear chain olefin skeleton isomerism
  • Purification process for preparing C4 materials for isobutene by C4 linear chain olefin skeleton isomerism
  • Purification process for preparing C4 materials for isobutene by C4 linear chain olefin skeleton isomerism

Examples

Experimental program
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Effect test

Embodiment 1

[0082] Example 1 Purification process of C4 material after etherification in refinery

[0083] This embodiment provides a purification process for C4 material after etherification in a refinery, and its process is as follows figure 1 shown. The flow rate of the C4 material after etherification in the refinery used in this embodiment is 12 tons / h, the concentration of n-butene is about 47%, and there is no carbonyl sulfide. Its main composition is shown in Table 2.

[0084] Table 2

[0085] name

Content / w%

name

content

Propylene

0.01

Total sulfur (calculated as sulfur)

20ppm

propane

2.0

MTBE

70ppm

[0086] name

Content / w%

name

content

Isobutane

40.1

Acetonitrile+propionitrile+NH 3

2ppm

n-butane

8.61

chlorine

2ppm

Isobutylene

1.51

arsenic

40ppb

C 5 +

1.1

h 2 o

300ppm

Methanol

0.1

...

Embodiment 2

[0096] Example 2 Purification process of C4 material after etherification in refinery

[0097] This embodiment provides a purification process for C4 material after etherification in a refinery, and its process is as follows figure 2 shown. The flow of C4 material after etherification in the refinery used in this embodiment is 25 tons / h, the concentration of n-butene is about 56%, and the content of COS is about 15ppm. The main composition is shown in Table 3.

[0098] table 3

[0099] name

content%

name

Content / w

Propylene

0.1

Total sulfur (calculated as sulfur)

60ppm

propane

3

MTBE

300ppm

Isobutane

30

Acetonitrile+propionitrile+NH 3

5ppm

n-butane

8

chlorine

3.5ppm

Isobutylene

1

arsenic

80ppb

C5+

1

h 2 o

500ppm

Methanol

0.6

COS

15ppm

Butadiene

0.1

Butene

margin

[...

Embodiment 3

[0114] Example 3 Purification process of C4 material after etherification in refinery

[0115] This embodiment provides a purification process for C4 material after etherification in a refinery, and its process is as follows image 3 shown. The flow rate of the C4 material after etherification in the refinery used in this embodiment is 35 tons / h, the n-butene is about 48%, and the COS content is about 7ppm. The main composition is shown in Table 4.

[0116] Table 4

[0117] Element

wt%

carbon two

0.226

[0118] Element

wt%

propane

1.316

Propylene

0.7965

Isobutane

35.877

n-butane

11.238

Butene

margin

Isobutylene

2.2105

carbon five

0.438

Butadiene

0.203

other

0.4925

total sulfur

55.40ppm

chlorine

3.7ppm

Arsenide

150ppb

h 2 o

500ppm

[0119] The purification process of the ab...

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Abstract

The invention relates to a purification process for producing C4 materials in an oil refinery, which comprises the following steps in any order to produce the C4 materials in the oil refinery: a, passing through a fibrous membrane reactor taking alkaline solution as working solution; b, passing through refined desulfurization reactor with a refined desulfurizer; c, passing through a hydrogenationbutadiene removal reactor with a noble metal selective hydrogenation catalyst; d, passing through an arsenic and phosphorus removal reactor with an arsenic and phosphorus removal agent; e, passing through a dechlorinating reactor with a dechlorinating agent; and f, passing through an oxygen-containing and nitrogen-containing compound removal reactor with oxygen-containing and nitrogen-containing compounds. After being purified by the process, the C4 materials etherified in the oil refinery can meet the requirements of the process for producing the isobutene by the butylene isomerism and catalysts.

Description

technical field [0001] The invention relates to a purification technology for low-carbon olefins in the field of petrochemicals, in particular to a purification process for C4 materials produced in Shanshan refineries for isobutene production from straight-chain C4-olefins. Background technique [0002] About 70w% of gasoline in China comes from catalytic cracking (FCC) gasoline, and catalytic gasoline has high sulfur content and low alkane number. Therefore, the current FCC gasoline needs desulfurization and addition of methyl tert-butyl ether (MTBE) to meet high gasoline standards. MTBE) to reduce the sulfur content in gasoline and increase the octane number of gasoline, the production of MTBE is very important to increase the octane number of gasoline in China. Most of the nearly 200 refineries currently have MTBE production units. [0003] The production of MTBE is the etherification of isobutene and methanol under the action of a catalyst to generate MTBE. The isobuten...

Claims

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Application Information

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IPC IPC(8): C10G67/14
Inventor 周红军周广林吴全贵
Owner CHINA UNIV OF PETROLEUM (BEIJING)
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