Process for Purifying HBr in Hydrocarbons
The present invention provides a method for separating HBr from HBr-containing hydrocarbons (alkenes, aromatics and/or alkanes) to purify the hydrocarbons. Reacting a silica supported metal oxide solid material (MO x /SiO 2 , MO x =MgO, CoO, Co 2 O 3 , CuO and mixture thereof) with HBr in HBr-containing hydrocarbons, so as to ensure that the concentration of HBr is reduced to below 1.87×10 −16 , and then oxidizing the solid material which reacted with HBr in oxygen or air to regenerate MO x /SiO 2 , meanwhile Br 2 is recycled. Therefore, the purpose of continuous purification of hydrocarbons can be achieved.
1 . A method for separating HBr from HBr-containing hydrocarbons, comprising:
a) providing a container and a solid material composed of at least one metal oxide and a support therein; contacting HBr-containing hydrocarbons with the solid material at a certain temperature; reacting the metal oxide with HBr to produce metal bromide and water; directing the hydrocarbons into a storage tank;
b) switching HBr-containing hydrocarbons to another similar container when metal oxide exhausts, to perform the process a); purging first container by steam; directing oxygen or air into first container, regenerating metal oxide at a certain temperature and recycling Br 2 ;
c) connecting two or more such containers by switch valve and thereby forming a purification system, cycling the process a) and process b) and HBr is separated from HBr-containing hydrocarbons.
2 . A method as claimed in claim 1 , wherein said hydrocarbons are alkanes, alkenes and/or aromatics.
3 . A method as claimed in claim 1 , wherein said metal oxide is selected from MgO, CoO, Co 2 O 3 , CuO and mixture thereof.
4 . A method as claimed in claim 3 , wherein said metal oxide is prepared by soaking the support in the solution of one or more acetate, nitrate and/or bromide of Mg, Co and Cu, and then drying and calcining them.
5 . A method as claimed in claim 1 , wherein said support is silica.
6 . A method as claimed in claim 1 , wherein said silica is commercial silica or prepared from silicates, SiCl 4 or silica ester.
7 . A method as claimed in claim 1 , wherein the step of contacting HBr-containing hydrocarbons with the solid material is carried out at a temperature of between about 100 □ and about 600 □.
8 . A method as claimed in claim 7 , wherein the step of contacting HBr-containing hydrocarbons with the solid material is carried out at a temperature of between about 150 □ and about 400 □.
9 . A method as claimed in claim 8 , wherein the step of contacting HBr-containing hydrocarbons with the solid material is carried out at a temperature of between about 170 □ and about 300 □.
10 . A method as claimed in claim 1 , wherein the step of regenerating metal oxide is carried out at a temperature of between about 250 □ and about 600 □.
11 . A method as claimed in claim 10 , wherein the step of regenerating metal oxide is carried out at a temperature of between about 300 □ and about 500 □.
12 . A method as claimed in claim 11 , wherein the step of regenerating metal oxide is carried out at a temperature of between about 320 □ and about 450 □.
13 . A method as claimed in claim 1 , wherein the purification system is composed of 2˜8 containers filled with the solid material connected by switch valve.
14 . A method as claimed in claim 13 , wherein the containers are columnar fixed bed reactors.