Process for cleaner production of chlorinated rubber without using carbon tetrachloride and water

• US 8,268,931 B2
• Filed: 06/24/2008
• Issued: 09/18/2012
• Est. Priority Date: 05/23/2008
• Status: Active Grant

• Current Assignee: Bolin Tong
• Original Assignee: Bolin Tong
• Inventors: Tong, Bolin
• Primary Examiner(s): Rabago, Roberto
• Application Number:
  US12/992,807
• Publication Number:
  US 20110071260A1
• Time in Patent Office: 1,547 Days
• Field of Search: 525/332.3, 525/333.1, 525/356
• US Class Current: 525/332.3
• CPC Class Codes: C08C 19/12 Incorporating halogen atoms into the molecule
• CPC Class Codes: C08C 19/18 by reaction with hydrocarbons substituted by halogen

Abstract

The present invention relates to a green technology to produce chlorinated rubber without using carbon tetrachloride and water by using 1,1,2-trichloroethane as the solvent and iodine as the catalyst. The natural rubber reacts with an excessive amount of gaseous chlorine at 60-100° C. for 3-8 hours and the product is then dried. The method of the present invention complies with the environmental requirements of “The Montreal Protocol on Substances that Deplete the Ozone Layer” by abandoning the usage of CCl₄. It also complies with the relevant regulations regarding ship-shell paints. Moreover, it is easy to carry out and is suitable for industrialization.

Claims

1. A method for making chlorinated rubber, comprising the steps of

using 1,1,2-trichloroethane as a solvent and iodine as a catalyst,

reacting natural rubber with an excessive amount of gaseous chlorine at 60-100°

C. for 3-8 hours in presence of the 1,1,2-trichloroethane and iodine, and

drying a product of the reaction.

2. The method as claimed in claim 1, wherein reaction time for chlorination is 3-4 hours and entrance gauge pressure is higher than 0 and between 0-0.1 MPa.

3. The method as claimed in claim 1, wherein the product is dried in a sealed container through spray drying or high speed centrifugal spray powder drying.

4. The method as claimed in claim 3, wherein said centrifugal spray powder drying is carried out at a top of a tower, its rotational speed is 10000-20000 revolutions per minute, and a mixture chamber with a temperature of 120-160°

C. is used to nebulize the product of the reaction into small particles, and the chlorinated rubber and the solvent are recovered.

5. The method as claimed in claim 1, further comprising the steps of

recovering the solvent in an exhaust gas through condensation,

absorbing hydrogen chloride by water to turn into hydrochloric acid, and

adding sodium hydroxide to turn the remaining chlorine into sodium hypochloride.

6. The method as claimed in claim 1, wherein the method is carried out in a sealed system.