Method for producing isobutylene from isobutanol
The purpose of the present invention is to provide a method that can produce, with high yield or high selectivity isobutylene by means of isobutanol dehydration-reaction. An isobutylene production method of a first embodiment of the present invention is a method for producing isobutylene by means of isobutanol dehydration-reaction, wherein isobutanol is reacted using a catalyst for which the BET specific surface area is within the range of 60 m 2 /g-175 m 2 /g, and the reaction is carried out under a reaction pressure of 50 kPa-750 kPa as the absolute pressure. An isobutylene production method of a second embodiment of the present invention includes: using a catalyst which is filled into a reaction chamber and for which the particle diameters of at least 90 mass % of the catalyst are within the range of 700 μm-1000 μm; setting the isobutanol concentration within a supplied reaction gas to 30 vol %-85 vol %; setting the weight hourly velocity (WHSV) of the isobutanol to 0.175 h −1 ˜20 h −1 ; and reacting isobutanol under a reaction pressure of 50 kPa-750 kPa as the absolute pressure.
1. A method for producing isobutylene comprising:
introducing a reaction gas containing isobutanol into a reactor, wherein the reaction gas further contains water in a content of 0.1 to 70 vol %; and
dehydrating the isobutanol,
at a reaction pressure of 50 kPa or more and 750 kPa or less as an absolute pressure,
by using an alumina catalyst having a BET specific surface area in a range of 60 m 2 /g or more and 175 m 2 /g or less and having a content of SiO 2 of less than 1.0 mass %.
2. The method for producing isobutylene according to claim 1 , wherein 90 mass % or more of the alumina catalyst has a particle size in a range of 700 μm or more and 10000 μm or less and
a weight hourly space velocity (WHSV) of isobutanol entering a reaction zone to be supplied is 0.175 h −1 or more and 20 h −1 or less.
3. The method for producing isobutylene according to claim 1 , wherein the BET specific surface area of the alumina catalyst is in a range of 65 m 2 /g or more and 170 m 2 /g or less.
4. The method for producing isobutylene according to claim 1 , wherein the BET specific surface area of the alumina catalyst is in a range of 69 m 2 /g or more and 162 m 2 /g or less.
5. The method for producing isobutylene according to claim 1 , wherein the reaction pressure is 75 kPa or more and 700 kPa or less as an absolute pressure.
6. The method for producing isobutylene according to claim 1 , wherein the reaction pressure is 100 kPa or more and 650 kPa or less as an absolute pressure.
7. The method for producing isobutylene according to claim 1 , wherein a temperature of the dehydration is in a range of from 108 to 500° C.
8. The method for producing isobutylene according to claim 1 , wherein a temperature of the dehydration is in a range of from 150 to 400° C.
9. The method for producing isobutylene according to claim 1 , wherein the content of SiO 2 in the alumina catalyst is less than 0.5 mass %.
10. A method for producing isobutylene comprising:
introducing a reaction gas containing isobutanol into a reactor, wherein the reaction gas further contains water in a content of 0.1 to 70 vol %; and
dehydrating the isobutanol,
at a concentration of isobutanol relative to all gaseous components entering a reaction zone to be supplied of 30 vol % or more and 85 vol % or less,
a weight hourly space velocity (WHSV) of isobutanol of 0.175 h −1 or more and 20 h −1 or less, and
a reaction pressure of 50 kPa or more and 750 kPa or less as an absolute pressure,
by using an alumina catalyst of which 90 mass % or more has a particle size in a range of 700 μm or more and 10000 μm or less.
11. The method for producing isobutylene according to claim 10 , wherein the concentration of isobutanol is 55 vol % or more and 80 vol % or less.
12. The method for producing isobutylene according to claim 10 , wherein the weight hourly space velocity (WHSV) of isobutanol is 0.2 h −1 or more and 18 h −1 or less.
13. The method for producing isobutylene according to claim 10 , wherein the weight hourly space velocity (WHSV) of isobutanol is 0.25 h −1 or more and 16 h −1 or less.
14. The method for producing isobutylene according to claim 10 , wherein a temperature of the dehydration is in a range of from 108 to 500° C.
15. The method for producing isobutylene according to claim 10 , wherein a temperature of the dehydration is in a range of from 150 to 400° C.