Polymer cracking

• US 5,481,052 A
• Filed: 04/08/1993
• Issued: 01/02/1996
• Est. Priority Date: 04/22/1992
• Status: Expired due to Fees

• Current Assignee: BP Chemicals Ltd. (BP PLC)
• Original Assignee: BP Chemicals Ltd. (BP PLC)
• Inventors: Wilson, David C., Hardman, Stephen, Leng, Stephen A.
• Primary Examiner(s): McFarlane, Anthony
• Assistant Examiner(s): WOOD, ELIZABETH D
• Application Number:
  US08/044,646
• Time in Patent Office: 999 Days
• Field of Search: 585/10, 585/241, 585/648, 585/653, 208/49, 208/50, 208/51, 208/52 R, 208/59, 208/60, 208/61, 208/67, 208/68, 208/69, 208/70, 208/72, 208/106, 208/107, 208/108
• US Class Current: 585/241
• CPC Class Codes: C10G 1/10 from rubber or rubber waste

Abstract

This invention relates to a process for cracking waste polymers in a fluidized bed reactor to produce vaporous products comprising primary products which can be further processed, eg in a steam cracker to produce olefins, characterized in that the vaporous products are treated to generate a primary product substantially free of a high molecular weight tail having molecular weights >700 prior to further processing. The removal of the high molecular weight tail minimizes fouling and prolongs the lifetime of the reactors used for further processing.

Claims

1. A process for cracking a polymer into hydrocarbon products which comprises contacting a polymer with a fluidized bed comprising (i) one or more particulate materials of quartz, sand, silica, ceramics, carbon black, and refractory oxides and (ii) an acidic catalyst in the presence of a fluidizing gas which does not oxidize the hydrocarbon products and at a temperature of 300°

-600°

C. and under pressure, said hydrocarbon products comprising saturated and unsaturated aliphatic and aromatic hydrocarbons;

a. which have less than 20% w/w of gases comprising C1-C4 hydrocarbons,

b. containing no more than 10% w/w of aromatic hydrocarbons associated with the weight of polyolefin polymers in the feed, and

c. which are substantially free of a high molecular weight tail comprising hydrocarbons having a molecular weight of at least 700 as measured by GPC,

the amount of high molecular weight tail product being minimized by fractionating the products to separate product with a high molecular weight tail and recycling said high molecular weight tail product back to the fluidized bed for re-cracking.

3. A process according to claim 1 or claim 2 wherein the hydrocarbon products are mixed with naptha and steam cracked to produce a product stream comprising ethylene.

4. A process according to claim 1 or claim 2 wherein the fluidising gas comprises at least one component of the products from the fluidised bed reactor which is recycled.

5. A process according to claim 1 or claim 2 wherein the fluidised bed reactor is operated at a temperature from 300°

-600°

C.

6. A process according to claim 1 or claim 2 wherein the weight ratio of polymer to the fluidising gas is in the range from 1:

1 to 1;

20.

7. A process according to claim 1 wherein the catalytic component of the fluidised bed is less than 40% wt of the total solids in the fluidised bed.

2. A process for cracking a polymer into hydrocarbon products which comprises contacting a polymer with a fluidized bed comprising one or more particulate materials of quartz, sand, silica, ceramics, carbon black, and refractory oxides in the presence of a fluidizing gas which does not oxidize the hydrocarbon products comprising saturated and unsaturated aliphatic and aromatic hydrocarbons:

a. Which have less than 20% w/w of gases comprising C1-C4 hydrocarbons,

b. containing no more than 10% w/w of aromatic hydrocarbons associated with the weight of polyolefin polymers in the feed, and

c. which are substantially free of a high molecular weight tail comprising hydrocarbons having a molecular weight of at least 700 as measured by GPC,

the amount of high molecular weight tail product being minimised by fractionating the products to separate the high molecular weight tail product and recycling said high molecular weight tail product back to the fluidized bed for re-cracking.