CN102909086A - Catalyst granule for synthesis ammonia - Google Patents
Catalyst granule for synthesis ammonia Download PDFInfo
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- CN102909086A CN102909086A CN201210386281XA CN201210386281A CN102909086A CN 102909086 A CN102909086 A CN 102909086A CN 201210386281X A CN201210386281X A CN 201210386281XA CN 201210386281 A CN201210386281 A CN 201210386281A CN 102909086 A CN102909086 A CN 102909086A
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- 239000003054 catalyst Substances 0.000 title claims abstract description 38
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 title claims abstract description 28
- 229910021529 ammonia Inorganic materials 0.000 title claims abstract description 14
- 238000003786 synthesis reaction Methods 0.000 title abstract description 6
- 239000008187 granular material Substances 0.000 title description 26
- 230000015572 biosynthetic process Effects 0.000 title description 3
- 239000002245 particle Substances 0.000 claims abstract description 22
- 239000011949 solid catalyst Substances 0.000 claims abstract description 5
- 238000006243 chemical reaction Methods 0.000 claims description 3
- 239000011248 coating agent Substances 0.000 description 5
- 238000000576 coating method Methods 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 241001391944 Commicarpus scandens Species 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- DVARTQFDIMZBAA-UHFFFAOYSA-O ammonium nitrate Chemical compound [NH4+].[O-][N+]([O-])=O DVARTQFDIMZBAA-UHFFFAOYSA-O 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000003317 industrial substance Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 235000017550 sodium carbonate Nutrition 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
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Abstract
一种用于合成氨反应中的固体催化剂颗粒,该颗粒的横截面外轮廓线呈连续的、光滑的七齿齿轮形状,该催化剂颗粒具有更高耐热耐压能力。
A solid catalyst particle used in ammonia synthesis reaction, the cross-sectional outline of the particle is in the shape of a continuous, smooth seven-tooth gear, and the catalyst particle has higher heat and pressure resistance.
Description
Technical field
The present invention relates to the solid catalyst particle that uses in a kind of ammonia synthesis reaction, be specifically related to the synthetic ammonia catalyst particle that a kind of main body is seven gear-like.
Background technology
Synthetic ammonia is important industrial chemicals, is mainly used to produce chemical fertilizer, nitric acid, ammonium salt, soda ash etc.As one of pillar industry of chemical industry, synthetic ammonia is the industry of a high energy consumption, poor benefit.Ammonia synthesis reaction is the process that a reversible heat release and gas volume dwindle, and considers from thermodynamics, reach or near equilibrium conversion, and catalytic reaction should be carried out under lower temperature and higher pressure.Yet the reduction of temperature can make reaction rate descend, and the raising of pressure can make again energy consumption greatly increase.The catalyst that mostly is greatly iron system that uses in the ammonia synthesis reaction now, operating temperature and pressure are all higher, and Large Scale Synthetic Ammonia Plants is normally at 400 ℃~500 ℃ and 20.0MPa~30.0MPa.The operating condition of this harshness is very high to the requirement of mechanical strength of solid catalyst particle, in case because the destroy integrity of catalyst granules will cause catalytic activity to reduce.Therefore the intensity that improves Iron Catalyst of Ammonia Synthesis is conducive to improve the stability of synthetic ammonia workshop section.
Summary of the invention
The technical problem that mainly solves among the present invention is to obtain a kind of high-intensity catalyst granules that has, with can be under the synthetic ammonia operating mode withstand high temperatures high pressure.Under hot conditions, catalyst granules can owing to expanded by heating, in the place of stress raisers, can be easy to break.According to mechanics principle, reduce the concentrated method of stress is to make the monnolithic case of member realize rounding off as far as possible.For this reason, the outer contour of the radial cross-section of catalyst granules main body is continuous, the smooth gear shape that is joined end to end and formed by the tangent minor arc of multistage among the present invention.According to the rule of in the higher mathematics smooth curve being judged, because the characteristic function of the curve of shape has the continuous derivative of single order like this, so be smooth curve.That is to say, the outer contour of catalyst granules cross section is smooth curve among the present invention.Having the frictional force of the in theory minimum except circle and minimum stress on such outer contour concentrates; And with respect to common cylinder, this gear-like of catalyst granules has higher specific area among the present invention.
Concrete technical scheme of the present invention comprises:
A kind of solid catalyst particle of gear-like, main body axial component are highly for H, and the radial cross-section outer contour of catalyst granules is continuous, smooth seven gear shapes, and the circumradius of outer contour is R, and inscribed circle radius is r.
Form above-mentioned catalyst granules main body radial cross-section continuous smooth gear-like outer contour be the curved section (as shown in Figure 1) with following feature: one group of quantity is 7, radius is the circle of β, around central point O, circular array in 0 ° to 360 ° scope; Do following three circles, be that (center of circle among Fig. 1 is O for the inscribed circle of outer contour, radius is the circle of r), and the circumcircle (such as the round S among Fig. 1) of 2 adjacent radiuses circle (such as the round P among Fig. 1 and circle Q) that is β, obtain another and organize quantity and be all 7 circle; Respectively from this circle of two groups, mutually circumscribed (mutually circumscribed with circle S such as circle P among Fig. 1 between any two, circle S is mutually circumscribed with circle Q), each circle is upper to form corresponding 2 point of contacts (such as the some A on the circle P among Fig. 1 and some B, some B on the circle S and some C), get the minor arc between these two point of contacts, these all minor arcs join end to end and consist of this continuously outer contour of smooth gear-like of cross section.
The various relevant parameters of above-mentioned formation catalyst particles grain character are of a size of:
R?=?3?mm?~5mm;
r?=?0.8R;
H?=?2R?~?2.2R;
β?=?0.2R。
The present invention compared with prior art, outline is smooth continuously, local stress is little, when improving the catalyst granules specific area, has more significantly improved the intensity of catalyst granules.
Description of drawings
Fig. 1 is that catalyst granules cross section outer contour of the present invention forms schematic diagram.
Fig. 2 is the embodiment of the invention 1 cross section outer contour schematic diagram (also being the cross section outer contour schematic diagram of embodiment 2 and embodiment 3 simultaneously).
The specific embodiment
Below in conjunction with drawings and Examples the present invention is further detailed:
Compared with prior art, the marked improvement of technical solution of the present invention has been to improve the intensity of catalyst granules, and intensity can be investigated by this index of wear rate.Adopt the small-sized seed-coating machine of BY-300A type that Shanghai Huanghai Sea medicine inspection Instr Ltd. produces (stainless steel coating pan diameter 200 mm processed, the coating pan inclination angle is 35 to spend) during the wear rate of specimen particle.During test, every kind of sample is randomly drawed 200, puts into coating pan, the coating pan rotating speed is controlled to be 60 rev/mins, keeps rotating speed to stop after 1 hour, takes out particle, the particle number W that the reading contour structures is complete, meter abrasion of particles rate ω=[(200-W)/200] * 100%.
Related catalyst granules of the present invention all is according to these particles architectural feature separately in the specific embodiment, adopts same material and facility to prepare.
The following examples only are used for the present invention that explains in detail, and limit the scope of the invention never in any form.
Embodiment 1
The cross sectional representation of catalyst granules such as Fig. 2 in the present embodiment, the design parameter size sees Table 1.Catalyst granules body height H=11 mm.The circumradius R of catalyst granules radial cross-section outer contour=5 mm, inscribed circle radius r=4 mm, radius β=1mm.This catalyst granules wear rate ω is 9.5%.
Embodiment 2
The cross sectional representation of catalyst granules such as Fig. 2 in the present embodiment, the design parameter size sees Table 1.Catalyst granules body height H=6.3 mm.The circumradius R of catalyst granules radial cross-section outer contour=3 mm, inscribed circle radius r=2.4 mm, radius β=0.6 mm.This catalyst granules wear rate ω is 7.5%.
Embodiment 3
The cross sectional representation of catalyst granules such as Fig. 2 in the present embodiment, the design parameter size sees Table 1.Catalyst granules body height H=8 mm.The circumradius R of catalyst granules radial cross-section outer contour=4 mm, inscribed circle radius r=3.2 mm, radius β=0.8 mm.This catalyst granules wear rate ω is 9%.
Table 1
| ? | H (mm) | R (mm) | r (mm) | β (mm) | ω % |
| Embodiment 1 | 11 | 5 | 4 | 1 | 9.5 |
| Embodiment 2 | 6.3 | 3 | 2.4 | 0.6 | 7.5 |
| Embodiment 3 | 8 | 4 | 3.2 | 0.8 | 9 |
Claims (6)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210386281XA CN102909086A (en) | 2012-10-13 | 2012-10-13 | Catalyst granule for synthesis ammonia |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210386281XA CN102909086A (en) | 2012-10-13 | 2012-10-13 | Catalyst granule for synthesis ammonia |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102909086A true CN102909086A (en) | 2013-02-06 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201210386281XA Pending CN102909086A (en) | 2012-10-13 | 2012-10-13 | Catalyst granule for synthesis ammonia |
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| Country | Link |
|---|---|
| CN (1) | CN102909086A (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20040185244A1 (en) * | 2001-08-01 | 2004-09-23 | Van Hasselt Bastiaan Willem | Shaped trilobal particles |
| US20080262115A1 (en) * | 2007-01-18 | 2008-10-23 | Hans Peter Alexander Calis | Catalyst, catalyst precursor, and catalyst carrier |
| CN202366710U (en) * | 2011-11-28 | 2012-08-08 | 孟莫克化工成套设备(上海)有限公司 | Sulfuric acid catalyst |
| CN202823400U (en) * | 2012-10-13 | 2013-03-27 | 安徽工程大学 | Catalyst granule for ammonia synthesis |
-
2012
- 2012-10-13 CN CN201210386281XA patent/CN102909086A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20040185244A1 (en) * | 2001-08-01 | 2004-09-23 | Van Hasselt Bastiaan Willem | Shaped trilobal particles |
| US20080262115A1 (en) * | 2007-01-18 | 2008-10-23 | Hans Peter Alexander Calis | Catalyst, catalyst precursor, and catalyst carrier |
| CN202366710U (en) * | 2011-11-28 | 2012-08-08 | 孟莫克化工成套设备(上海)有限公司 | Sulfuric acid catalyst |
| CN202823400U (en) * | 2012-10-13 | 2013-03-27 | 安徽工程大学 | Catalyst granule for ammonia synthesis |
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| PB01 | Publication | ||
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| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20130206 |