Catalyst for isomerizing butene-2 into butene-1

专利摘要:
Catalysts based on gamma alumina, consisting of gamma alumina stabilised by silica and containing oxides of bivalent or trivalent metals chosen from those of Group 2a and/or Group 8 and/or Group 3b and/or the Lanthanide Series, are disclosed. The catalysts are particularly active in isomerisation reactions.
公开号:SU1440330A3
申请号:SU833597798
申请日:1983-05-26
公开日:1988-11-23
发明作者:Форлани Орфео；Анциллотти Франческо；Нотари Бруно
申请人:Снампрогетти С.П.А (Фирма)；
IPC主号:

专利说明:

4 4
About WITH
with

s
the material is dried and calcined at 4 h. The resulting material contains 3.5 wt.% on J alumina (, 014; m 0.240).
Example 3 (for comparison). Carrying out the process as in Example 2, 20 g of alumina is impregnated with 15 cm of an aqueous solution. The invention relates to catalysts for isolating olefins, in particular for isomerizing butene-2 to butene-1.
The purpose of the invention is to increase the selectivity of the catalyst due to the additional content in its composition of a metal oxide selected from
the group including lanthanum, calcium, 10that holding 2.57 g of lanthanum nitrate,
barium, strontium, iron, when determined - Get a catalyst containing
divided content of components ka-5 wt.% on alumina, talizatora.Katalizatory obtained in the example of p and m, e 1. 20 g of gamma oxides 2 and 3 are tested in
aluminum (S.A. 200) is treated with butene-2 isomerization process. 15 cm of alcohol solution, containing the results of selective isomeric 0.75 g of dinasyl A 40 (40% trans-transformation of trans-butene-2- into butene-1 (ethylene orthosilicate of ethylene)) are listed in Table. one.
The mixture reacts for 2 hours at. In tab. 1-5 reaction conditions are next C, then it is dried and treated with 20 duct: T P 1 ata; colipar to hydrolyze the silanol of trans-butene-2 per unit
ny groups. Sustained drying and ob-: catalyst mass in 1 h is equal to 6. burned for 4 hours. Example 4. 20g gamma oxide
Thus obtained material, aluminum (specific surface area
containing 1.5% of SiO, impregnated with 25200) is treated with 15 cm of an alcohol of 15 cm of an aqueous solution containing a solution containing 0.75 g
5.90 g of lanthanum nitrate. Then propidinazyl A 40 (40% ethyl
tannin material is dried and burned with a solution of orthosilicate). The mixture was reacted at 500 ° C for 4 hours.
cuts at 50 ° C and then it is drained and
The resulting material is steamed with the aim of
is a gamma-alumina, stabilized with 1.5% SiO, contains LajO.B amount corresponding to the equation: mol La / jOj 0.664 mol SiO-i + 0.14; (b + c): a 0.0642 and b 0.025 per 100 g of catalyst (B 0.018; m 0.5).
This catalyst is fed to a reactor in which butene-2 is isomerized
hydrolysis of silanol groups. It is dried and calcined at 500 s for 4 hours.
The material thus obtained, 35 containing 1.5% SiO, is impregnated with 2.57 g of lanthanum nitrate as in Example 3.
A material consisting of gamma-alumina is obtained, stabilized by reaction at 40.5% SiO 2, and containing 5% ferric pressure and speed of use. catalyst (WHSU) 6.
The catalyst allows to obtain - The interdependence of the number of moles of butene-1 with the content of isobutene of the function of the number of moles of dioxides of silicon as follows: mol — 0.05 mol of SiO + 0.014; (b-i-c): a 0.0430; m 0,24, B 0,014.
Example 5 (for comparison). 20 g of silicified alumina.
140 ppm
After heat treatment for 24 hours at 1000 ° C, the catalyst has a surface area of 113, does not show a loss of activity after 40 cycles (332 hours in general) of the reaction and 40 cycles of regeneration (152 hours in general).
50
prepared according to example 4, is impregnated with an aqueous solution of lanthanum nitrate according to the method described in example 2. A material consisting of aluminum oxide, 1.5% SiO-j and 7.5% is obtained, Ba-zRz 0.32 mol SiO-i + 0.014;
prepared according to example 4, impregnated with an aqueous solution of lanthanum nitrate according to the method described in example 2. A material consisting of aluminum oxide, 1.5% SiO-j and 7.5% ba-zRz 0.32 mol SiO-i is obtained + 0.014;
Regeneration is performed at 540 C.
Example 2 (for comparison) 4-,. ","
20 g of gamma-alumina (with specificity (L + c): a 0.0527; m 0.666. Surface 200) are impregnated. Example 6 (for comparison), 15 cm of an aqueous solution containing 1.8 g of lanthanum nitrate . Then
A catalyst is produced in a manner analogous to that which consists of alumina.
the material is dried and calcined at 4 h. The resulting material contains 3.5 wt.% on alumina (, 014; m 0.240).
Example 3 (for comparison). Carrying out the process as in Example 2, 20 g of alumina is impregnated with 15 cm of an aqueous solution, coalesced at 50 ° C and then it is drained and
steam treated to
prepared according to example 4, is impregnated with an aqueous solution of lanthanum nitrate according to the method described in example 2. A material consisting of aluminum oxide, 1.5% SiO-j and 7.5% is obtained, Ba-zRz 0.32 mol SiO-i + 0.014;
-, ","
(B + c): a 0.0527; m 0.666. Example 6 (for comparison)
(B + c): a 0.0527; m 0.666. Example 6 (for comparison)
The catalyst is prepared as described above, consisting of alumite oxide
3
neither, stabilized with 1.5% SiOi and modified with 10% mol 0.664 mol SiO + 0.014; (B + c): a 0.0735; m 0.4.
Example 7. 20 g of alumina oxide is impregnated in Example 4 with an alcoholic solution of orthosilicate, as a result of which a material is obtained which, after treatment with water vapor and calcination, contains 3.8% SiOj.
This material is then impregnated with the required amount of lanthanum nirate solution so that a content of 5.0% is obtained. Thus, a catalyst is obtained containing 3.8 SiO and 5.0%. C on alumina, 0.0158 mol SiO + 0.014; (b + c): a 0.0872, m 0.265.
Example 8. A catalyst with a composition of 3.8% SiO and 7.5% on alumina was prepared analogously to Example 7, mol 3 0.143 Siffl 2 + + 0.014; (b + c): a 0.0989, m 0.270
Example 9 (for comparison). The catalyst composition of 3.8% SiOi and 10.0 on alumina is obtained analogously to Example 7, mol 0.233 mol SiO + 0.014; (b + c): a 0.111.
Example 10. A catalyst of 8% SiO and 5% on alumina is prepared in the manner described, mol 0.0098 x mol SiOj + + 0.0144; (b + c): a 0.1738.
Example 11. The catalyst composition of 8% SiO. and 7.5% 3 on alumina is prepared in the manner described. Mole La2.0c 0.0676 mol SiOi +
+ 0.014; (b + c): a 0.1829.
Example 12. The catalyst composition of 8% SiOi and 10.0% T. on alumina get in this way. Mole T. 0.1253 mole 0.014; (b + c): a 0.1883.
Example 13. The catalyst composition of 8% SiO g and 15% LajOj on alumina is obtained in the manner described above, yol 0.241 mol SiO-j + + p, 014; (B + c): a 0.2099.
Example 14. Using silicified alumina, prepared analogously to example 7, a catalyst is obtained by impregnating this rich aluminum oxide (3.8% SiOij) with an aqueous solution of a rare earth element acetate in such an amount that the final ready-to-use catalyst contains 10











/.
five
about
50
five
0
five
rare earth oxide. Mole REE oxide of average molar mass 145 0.0174 mol SiO + 0.016.
In tab. Figure 2 shows the test data for the catalysts paramilitary in Examples 4-14, and indicates the specific surface area of the catalysts after their heat treatment for 24 hours at.
In tab. 2-5 linear butenes are always present in quantities corresponding to thermodynamic equilibrium at the reaction temperature.
Example 15. The catalyst composition of 1.5% SiO-2 + 2.5% CaO on alumina is prepared in the manner described. Calcium is introduced in the same way as lanthanum in the form of calcium nitrate solution, mol CaO 0.584 mol SiOj + + 0.030; (b + c): a 0.0739.
Example 16. A catalyst with a composition of 1.5% SiO- + 5.0% CaO on an oxide is prepared, mol CaO 2.372 mol SiO-2 + 0.030; (b + c): a, 0.1214.
Example 17. A catalyst of the composition of 1.5% SiO + 7.5% CaO on alumina, mol CaO 4.156 mol SiO7 + 0.030 (b + c) is prepared: a 0.4409.
Example 18. A catalyst of composition 3.8% SiOi + 2.5% CaO on alumina, mol CaO 0.2306 mol SiO 0.030; (b + c): a 0.1170 ..
Example 19. A catalyst of composition 3.8% SiO + 5.0% CaO on alumina, mol CaO 0.9360 mol SiO + 0.030 (b + c) is prepared: a 1660.
Example 20. A catalyst of composition 3.8% SiO + 7.5% CaO on alumina, mol CaO 1, .6414 mol SiOi + 0.030; (b + c): a
 0.2146.
In the case of CaO, a value of 0.030 is the number of moles of isobutene within these limits when using 0 alumina, which has not been stabilized by silica.
The results of isomerization of trans-butene-2 to butene 1 are given in Table. 3. All the catalysts used in examples 2-20 are subjected to aging tests, including 40 reaction cycles (332 hours in total) and 40 cycles of regeneration (152 hours in total) without
five
loss of catalytic activity. Regeneration is carried out at 540 ° C,
Example 21. A catalyst with a composition of 1.5% SiOj + 4.0% BaO on alumina is prepared in the manner described (barium is introduced in the same way as calcium in the form of barium nitrate solution), mole BaO 0.240 mol SiO / j + -I- 0.020; (b-i-c): a 0.0551.
Example 22, Prepare a catalyst composition of 1.5% SiO / i 8,0% Bao on alumina, mol BaO 1,280 mol SiO + 0,020; (b + c): a "0.0777.
Example 23 A catalyst composition of 3.8% SiOt 4.0 BaO on alumina is prepared in the manner described, mol BaO 0.093 mol SiO + f 0.020; (b + c): a 0.09890.
Example 24. The catalyst composition of 3.8% SiO + 8.0% BaO on alumina is prepared as described, mol BaO 0.5055 SiOi + + 0.020; (b + c): a 0.12281.
Example 25. The catalyst composition of 3.8% SiOj + 3.5% SrO on alumina is prepared in the manner described, mol Sr 0.2192 mol SiOi + f 0.010; (b + c): a 0.1080.






0.020 is the B value where BaO is used to neutralize alumina that is not stabilized by silica.
Example 34. The catalyst composition of 5.0% SiO and 5% Fe203Ha gamma-alumina is prepared as described, mol 0.1610 mol 0.018; (B + c): a 0.1301.
Example 35. The catalyst of composition 5.0% SiOj and 7.5% on gamma-alumina is prepared analogously to the described, mole Fei03. Trans-isomerization results. mol SiO 0,018; (bVc): a
ten-2 in butene-1 are given in table. four.
Example 26 A catalyst of composition 1.5 SiOii and 2.5% 3 on alumina is prepared in the manner described (iron is introduced in the form of an aqueous solution of iron nitrate), mol 3 0.092 mol SiO-z + 0.018, (b + c),: a "0,0432 (0,018 - the value of B when using)).
 0.1521.
In tab. 5 presents the results of the tests in examples 26-35,,. 40 Example 36. In Example 1, a catalyst is obtained consisting of gamma alumina stabilized with 1.5% SiO and containing 3 in the amount corresponding to the equation and lll / n J V / f APPL & “Lh / / .. n t lf4 f
„0-t„ g J 45 to the note: mol La.O 0.241 mol SiOi +
Example 27 The catalyst is n /-.n Alpp t. 4 о о о, 7 l. 0.014; (B + c): a 0.2099, b
. va 1.5% SiO and 3.8% Fe, gamma II ii r (
  ge 0.133 per 100 g of catalyst,
alumina is prepared as ana
logically described, moles of FejOs-silica add an image of 0.352 mol + 0.018; (b + c): ca. 20 g of gamma alumina
0.0525. ml of alcohol solution, containing Example 28. Catalyst conjoining 5.19 g of dinasyl A 40. Impregnation
tava 1.5% SiOa and 5.0% Fe 3 on gamma hydroxy lanthanum is carried out using
de aluminum is prepared as described by 15 kp of an aqueous solution containing
thus, mol Fe / jO 0.5376 mol 55 0 38 g of lanthanum nitrate, 0.018; (L + s): a "0.0615, the catalyst is loaded into the reactor.
Example 29, Catalyst Soy — in which trans-butene-2 isomerized
tava 3.8% SiOi and 2.5% on gamma conditions in example 1. Catalyst
alumina prepare analog-able to form butene-1 with
described as mole
 0.0363 mol SiOj + 0.018; (b + c): a 0.0860.
Example 30. The catalyst composition of 3.8% SiOj and 3.8% prepared as follows, mol 0,09320 mol SiOi + 0,018.
Example 31. The catalyst composition is 3.8% SiO and 5.0% FejO s are prepared similarly to the described mole of Fe O. “0.2120 mol SiO + 0.018; (b + c): a 0,01059.
Example 32. A catalyst of 5.0% SiOj and 2.5% on gamma alumina is prepared as an opium. in this way, mol 0.0276 mol SiO- + 0,018; (b + c): a: 0.1091.
Example 33. The catalyst soy-, tava 5.0% SiO and 3.8% on gamma-alumina is prepared in the manner described, mol 0.0708 mol SiOi + 0, OG8; (B + c): a 0.1200.
Example 34. The catalyst composition of 5.0% SiO and 5% Fe203Ha gamma-alumina is prepared as described, mol 0.1610 mol 0.018; (B + c): a 0.1301.
Example 35. Catalyst of composition 5.0% SiOj and 7.5% on gamma-alumina is prepared ana0
five
0
 0.1521.
In tab. 5 presents the results of the tests in examples 26-35,,. Example 36. In Example 1, a catalyst is obtained consisting of gamma-alumina stabilized with 1.5% SiO and containing 3 in the amount corresponding to the equation L p t lf4 f
isobutene content in the range of 200 ppm (0.02%) relative to butene-1. After heating for 24 hours at 1000 ° C, the catalyst has a specific surface of 145.
Example 37. In Example 1, a catalyst is obtained, which consists of gamma-alumina stabilized with .1.5% SiOo and containing La; in the amount of the equation: mol 0.32 mol SiO-z + 0.014; (b + c): a 0.0527, b 0.025 per 100 g of catalyst.
The impregnation with lanthanum is carried out using 15 ml of an aqueous solution containing 4.38 g of lanthanum nitrate.
The catalyst is loaded into a reactor in which, under the conditions of Example 1, trans-butene is isomerized.
Butene-1 with isobutene content of 490 ppm (0.029%) can be obtained on the catalyst. After heating for 24 hours, the catalyst has a specific surface area of 134.
Example 38 Similarly to Example 1, a catalyst is obtained, which consists of gamma-alumina.
stabilized with 1.5% SiO and co 30 water t 4 h at 500 C.
keeps CaO in an amount corresponding to the equation: mole CaO 4.156 mol SiOj + 0.03; (b + c): a 0.178 and b 0.025 per 100 g of catalyst.
Calcium impregnation is carried out using 15 ml of an aqueous solution containing 6.9 g of calcium nitrate. Drying and roasting is carried out at 500 seconds for 4 hours.
The catalyst obtained is loaded into a reactor in which, under the conditions of Example 1, trans isomerization is carried out.
butene-2. With the help of the catalyst, py 1 produces a catalyst that radiates butene-1 containing isobut — consists of gamma-alumina, for 300 ppm (0.03%) relative to 45 stabilized by 3.8% SiOi, and
.contains BaO in the amount corresponding to the equation: mole BaO 0.5055
butene-1, After heating for 24 hours at 1000 ° C, the catalyst has a specific
surface 136.
Example 39. Analogously to example 1, a catalyst is obtained, which consists of gamma-alumina, stabilized with 3.8% SiO and containing CaO in an amount corresponding to the equation: mol CaO 0.6414 mol SiOa + 0.03; (b + c): a 0.2146 and b 0.063 per 100 g of catalyst.
Treatment of silica with 20 g of gamma alumina with an alcohol solution (15 ml) containing
403308
1.9 dinasyl A 40, and calcium impregnation is carried out using 15 ml of an aqueous solution containing 7.12 calcium nitrate.
The drying and calcination is carried out by heating for 4 hours at 500 s.
The catalyst is loaded into a reactor in which isomerization is carried out under the conditions given in 10 of Example 1
trans-butene-2. The catalyst obtained allows the preparation of butene-1 with isobutene content of 150 ppm (0.015%) relative to butene-1. After 15 heating for 24 hours at 1000 ° C, the catalyst has a specific surface of 150.
Example 40. In Example 1, a catalyst is obtained, which consists of 20 gamma-alumina, stabilized with 1.5% SiO and containing BaO in an amount corresponding to the equation: mole BaO 0.24 mole 510-2 + + 0.02; (B + c): a 0.0551 and b 0.025 5 per 100 g of catalyst.
Barium impregnation is carried out using 15 ml of an aqueous solution containing 1.45 g of barium nitrate. Drying and roasting (burning) about
The resulting catalyst is loaded into a reactor in which transbutene-2 isomerization is carried out analogously to example 1.
The catalyst makes it possible to produce butene-1 with isobutene content of 260 ppm (0.026) relative to butene-1.
After heating for 24 hours at 1000 ° C, the catalyst has a specific surface area of 192.
Example 41. Similarly, when taken in South; (L + c): a = 0.12281 and b = 0.063 per 100 g of catalyst.
Silicon dioxide is injected by treating 20 g of gamma alumina with 15 ml of an alcohol solution containing 1.9 g of dinasyl A 40.
Barium impregnation is carried out using 15 ml of an aqueous solution containing 3.1 barium nitrate.
Drying and roasting are carried out for 4 hours at 500 ° C.
The catalyst obtained is loaded into a reactor in which trans-butene-2 isomerization is carried out under the conditions of Example 1. Using gru 1, a catalyst is obtained which
catalyst can be obtained butene-1 consists of gamma-alumina,
with isobutene 230 ppm stabilized 3.8% SiO and
(0.023%) relative to butene-1. containing in an amount, After heating for 24 hours at 1000 °. Candle equation: mol
the catalyst has a specific surface of -100.212 mol SiOi + 0.018, where (H + c):
154.: a 0,1059 and b 0,063 per 100 g
Example 42. In Example 1, under the same conditions, a catalyst is obtained, which consists of gamma-alumina, stabilized with 1.5% SiO .j, an alcohol solution containing and containing Fe-jO jB amount, leaving 1.9 g of dinasyl A40.
catalyst.
Silicon dioxide is introduced by processing 20 g of gamma alumina 15 ml
20
by the equation: mole
 0.352 mol SiOa + 0.018; (YS): a "
 0.0525 and b 0.025 per 100 g of catalyst.
The impregnation with iron is carried out using 15 ml of an aqueous solution containing 4.14 g of iron nitrate. Drying and calcination are carried out for 4 hours at.
The catalyst obtained is loaded into a reactor in which trans-butene-2 isomerization is carried out under the conditions of Example 1. The catalyst obtained makes it possible to obtain butene-1 with an isobutane content of 430 ppm (0.043%). After treatment for 24 hours, the catalyst has a specific surface of 129.
Example 43. In Example 1, a catalyst is obtained, which consists of gamma-alumina stabilized with 5% SiO and contains
The impregnation with iron is carried out using 15 ml of an aqueous solution containing 5.57 g of iron nitrate. Drying and calcining the wire for 4 hours at.
The catalyst obtained is loaded into a reactor, in which, under the conditions indicated in Example 13, iso-25 trans-butene-2 is measured.
The catalyst obtained makes it possible to obtain butene-1 with an impurity of isobutene 420 ppm (0.042%) relative to butene-1.
After heating for 24 hours at 1000 ° C, the catalyst has a specific surface of 141 m / g.
Thus, the proposed catalyst for conversion of 100% has a 35 high selectivity for butene-1 99.8-99.9%.

权利要求:
Claims (1)
[1]
Invention Formula
in the amount of the equation: mol 0.351 mol SiO + 0.018; (b + c): a 0.1521 and b - 0.083 per 100 g of catalyst.
Silicon dioxide is introduced into the catalyst by treating 20 g of gamma alumina with 15 ml of an alcohol solution containing 2.5 and dinazyl A40.
The impregnation with iron is carried out using 15 ml of an aqueous solution containing 8.7 iron nitrate. Drying and calcination were carried out for 4 hours at 500 ° C. The resulting catalyst was loaded into a reactor in which, under the conditions given in Example 1,
40 The catalyst for isomerization of butene- 2 to butene-1, including silicon dioxide and gamma-alcumin oxide, is characterized in that, in order to increase the selectivity of the mash catalyst, it additionally contains a metal oxide selected from the group comprising lanthanum, calcium, barium, strontium, iron, with the following content of components, wt.%: 50. Metal oxide 2,5-10,0 Silicon dioxide 1,5-8,0 Gamma-alumina Else
at the same time, the composition of the catalyst corresponds to the isomerization of trans-butene-2. gg formula
The catalyst allows to obtain butene-1 containing isobutene a-Al Oj b SiO-i C-MexOy, 350 ppm (0.035%) relative to butene-1. After heating for 24 hours at where is a metal oxide, a selected 1000 ° C catalyst has a specific surface of 150 m / g.
Example 44. Similar to the alcohol-containing solution containing 1.9 g of dinazyl A40.
catalyst.
Silicon dioxide is introduced by processing 20 g of gamma alumina 15 ml
The impregnation with iron is carried out using 15 ml of an aqueous solution containing 5.57 g of iron nitrate. Drying and calcination are carried out for 4 hours at.
The catalyst obtained is loaded into a reactor, in which the isomerization of trans-butene-2 is carried out under the conditions specified in Example 13.
The catalyst obtained makes it possible to obtain butene-1 with an isobutene impurity of 420 ppm (0.042%) relative to butene-1.
After heating for 24 hours at 1000 ° C, the catalyst has a specific surface area of 141 m / g.
Thus, the proposed catalyst for conversion of 100% has a high selectivity for butene-1 99.8-99.9%.
Invention Formula
The catalyst for isomerization of butene-2 to butene-1, which includes silicon dioxide and gamma-oxide of alcmini, is characterized by the fact that, in order to increase the selectivity of the catalyst, it additionally contains a oxide of a metal selected from the group including lanthanum, calcium, barium, strontium, iron, with the following content of components, wt.%:. Metal oxide 2,5-10,0 Silicon dioxide 1,5-8,0 Gamma-alumina Else
b, c
1114AOZZO
him from the group above
- the number of moles, respectively, Al-iOj, SiO-z
Me 0
 0
(in the form of REE oxides)
ZO
12
, moreover, with m b + B, where B 0,01A-a, P:., b 0,025-0,14, m
 0.24-0.666, --3
0,01059-0,4409. Table 1
table 2
Table 3
Table 4
15
1440330
16 Continuation of table 5

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引用文献:

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法律状态:

优先权:

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申请号 | 申请日 | 专利标题

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IT21512/82A|IT1152198B|1982-05-27|1982-05-27|ALBUMINE RANGE CATALYST AND ITS PREPARATION METHOD|

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