CN1140628A - Handling method for fixed bed reactor catalyst and its main equipment - Google Patents
Handling method for fixed bed reactor catalyst and its main equipment Download PDFInfo
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- CN1140628A CN1140628A CN 95107485 CN95107485A CN1140628A CN 1140628 A CN1140628 A CN 1140628A CN 95107485 CN95107485 CN 95107485 CN 95107485 A CN95107485 A CN 95107485A CN 1140628 A CN1140628 A CN 1140628A
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Abstract
In the present invention, catalyst handling system with grain sucking pipe as main part is used in loading and unloading catalyst or filling grains in the diameter not larger than 15 mm. At the inlet end of the grain sucking pipe, there are three flat teeth spaced by 120 deg, and they are used to dredge the reactor pipe by eliminating the jammed or adhered catalyst grains. The said catalyst handling system and method are also suitable for loading and unloading catalyst in the protective atmosphere.
Description
The present invention relates to a kind of handling method of fixed bed reactor catalyst, exactly is filling and unloading method and capital equipment thereof about catalyst in the upright multitube fixed bed reactors.
The air-flow of particle is carried, and widely each relevant industrial, agricultural, traffic and transportation sector are used, but in chemical system, is applied to the filling of catalyst in the upright multitube fixed bed reactors and draws off report less.Catalyst in the upright multitubular reactor draws off; the unloading methods down that adopt more; promptly unloading catalyst mouth place at reactor bottom emits; this catalyst method of unloading is usually less because of reaction tube diameter; the reaction tube endoparticle is built bridge, is bondd and stop up or adhere to tube wall; cause catalyst to draw off endless; be difficult to smooth operation; especially catalyst is carried out inert gas shielding and need sieve or when separating catalyst and filler particles at needs; because equipment is huge; dust pollution is serious, brings bigger trouble to operating personnel.RO79865 discloses the Apparatus and method for that catalyst draws off continuously in a kind of barrel reactor, this method is to adopt the cyclone separator and the vacuum suction method of two blocked operations to operate continuously, draw off the dead catalyst in the barrel reactor, but do not relate to upright multitubular reactor, also relate to filling and do not build bridge easily when drawing off catalyst, problem such as obstruction.Br75-06251 discloses a kind of upright multitubular reactor catalyst discharge equipment and has improved one's methods, this patent proposes, a removable tube head is connected on the reaction tube outlet, pass this tube head and insert a lance utensil to reaction tube, vacuum suction, the interior bed catalyst granules of reaction tube is flowed, force mediation to be built bridge, remove and stop up, reach the purpose that draws off catalyst smoothly, whole bed catalyst stream moves in the reaction tube in order to make, need air mass flow big, air-extractor is big, the energy consumption height, and operation is also inconvenient.
The unloading method that the purpose of this invention is to provide a kind of upright multitube fixed bed reactor catalyst.
Another object of the present invention provides a kind of packing method of upright multitube fixed bed reactor catalyst.
The 3rd purpose of the present invention provides a kind of critical piece-grain sucting tube that is used for loading or drawing off antigravity system.
The present invention realizes by following proposal:
When drawing off catalyst, by the negative-pressure air-flow that vacuum suction device produces, to the catalyst bed bed boundary, carrying catalyst granules secretly by the annular space between reaction tube and the grain sucting tube, enter the gas-solid separator sedimentation through grain sucting tube and be collected in its underpart, intermittently take out then; Meticulous catalyst dust is then captured through dust filter unit with negative-pressure air-flow, and tail gas is discharged by vacuum system.
When loading catalyst, negative-pressure air-flow by the vacuum suction device generation, by grain sucting tube catalyst granules is carried secretly from catalyst container to catalyst filling funnel, after catalyst reaches predetermined quantity, stop to bleed, open the switch of catalyst filling funnel bottom, catalyst is promptly put into reaction tube through dress agent pipe.
The critical piece grain sucting tube that is used for the loading, unloading antigravity system, its arrival end have the flat tooth at 120 ° at all each intervals, three gardens, are used for dredging the reaction tube catalyst particles and build bridge, eliminating particle bonding, wall built-up and clogging.
Describing the upright multitube fixed bed reactors of the present invention in detail below in conjunction with accompanying drawing draws off and the method for loading catalyst and the structure that is used for loading or drawing off antigravity system critical piece grain sucting tube (1).
Fig. 1 draws off the schematic flow sheet of catalyst granules for the present invention.
Fig. 2 is the schematic flow sheet of loading catalyst particle of the present invention.
Fig. 3 is grain sucting tube (1) arrival end explosion views.
By shown in Figure 1, drawing off antigravity system is to be made of following parts and equipment: with removable Pass the concentric of coupled reaction pipe (3) arrival end with the arrival end of the metal grain sucting tube (1) that rotates Gas flows into out threeway (2), directes reach the catalyst bed bed boundary in the reaction tube (3), grain sucting tube (1) The other end be connected the top of (5) and dust by inhaling a grain flexible pipe (4) with gas-solid separator (5) Filter (7) links to each other, and valve (10) is equipped with in the bottom of (5), holds by row's grain pipe (9) and catalyst Device (6) links to each other. Dust filter unit (7) links to each other with vacuum suction device (8), valve 11 and the same motive Flowing into out threeway (2) links to each other.
The operating procedure that the present invention draws off catalyst is as follows: the arrival end of grain sucting tube (1) is passed Gas flows into out in threeway (2) the insertion reaction tube (3) with one heart, directes reach the bed interface of catalyst, beats Open with concentric gas and flow into out the valve (11) that threeway (2) links to each other, start vacuum suction device (8), By the negative-pressure air-flow of (8) generation, by the annular space between reaction tube (3) and the grain sucting tube (1) To the catalyst bed bed boundary, move up and down at the interface grain sucting tube or regulate negative-pressure air-flow at bed Speed, negative-pressure air-flow are being carried catalyst granules secretly and are being entered gas-solid separator (5) through inhaling grain flexible pipe (4) And being collected in its bottom, meticulous catalyst dust is through the bleeding point at gas-solid separator (5) top Overflow, capture through dust filter unit (7) again, intermittently take out from filter (7), open (5) end The valve (12) of the valve of section (10) and catalyst container (6) top, catalyst is through between row's grain pipe (9) Have a rest and be disposed in the catalyst container (6).
If need under the inert gas shielding condition, draw off catalyst, unload antigravity system In, valve (11) directly can be linked to each other with inert gas source (such as nitrogen).
By shown in Figure 2, the loading catalyst system is made of following parts and equipment: with grain sucting tube (1) arrival end inserts catalyst container (6) and extends catalyst interface, and the other end is by inhaling Grain flexible pipe (4) links to each other with Catalyst packing funnel (14), and filling funnel (14) bottom is by the dress agent Pipe (15) passes concentric gas and flows into out in threeway (2) the insertion reaction tube (3), filling funnel (14) Top flow into out threeway (2) with dust filter unit (7) and concentric gas and be connected dust-filtering Device (7) communicates with vacuum suction device (8).
The concrete operation step of loading catalyst of the present invention is: open and inhale grain flexible pipe (4) and catalysis Valve (16) between the agent filling funnel (14) is closed (14) following valve (17) and (14) The valve (18) of side top and flow into out threeway (2) and powder with (14) top, concentric gas The valve (19) that dirt filter (7) links to each other inserts grain sucting tube (1) in the container that catalyst is housed (6) in, direct reach catalyst interface, open the valve (12) of (6) top, start the vacuum suction dress Put (8), move up and down at the bed interface grain sucting tube head or bleeding regulating air velocity make (8) negative-pressure air-flow that produces is being carried catalyst granules secretly through grain sucting tube (1) and is being inhaled grain flexible pipe (4) Enter Catalyst packing funnel (14), meticulous catalyst dust is from the top bleeding point of (14) Overflow, capture intermittently through dust filter unit (7) and take out, in Catalyst packing funnel (14) When catalyst amounts reaches predetermined value, stop to bleed, open valve (18,19), make system extensive Multiple normal pressure, valve-off (16) is opened valve (17), urging in the Catalyst packing funnel (14) Change agent, pass concentric gas through dress agent pipe (15) and flow into out threeway (2) and put into lentamente reaction tube (3) In.
If need to be under the inert gas shielding condition loading catalyst, at loading catalyst be In the system, can be with the valve (12) of catalyst container (6) top, on Catalyst packing funnel (14) side The valve (18) of side directly links to each other with inert gas source (such as nitrogen).
In the said loading, unloading method of the present invention, catalyst grain size≤15mm also can load and unload The inert filler of same granularity.
In the said loading, unloading method of the present invention, between each parts of loading and unloading antigravity system be Connect by rubber components sealing or pipeline.
By shown in Figure 3, grain sucting tube (1) arrival end has the flat tooth at 120 ° at all each intervals, three gardens, and the height of flat tooth (h) is about the diameter (d of grain sucting tube (1)
b) 1/3rd (be h=1/3d
b).
Grain sucting tube (1) is the crux parts that are used for loading or drawing off antigravity system, the caliber (d of grain sucting tube (1)
b) less than the caliber (D of reaction tube (3)
Ra), its length is greater than the about 5-10% of reaction tube (3) length.Grain sucting tube (1) normally is formed by connecting by many short metal tube spiral shell mosquitos, can about, the rotation of move left and right, both forward and reverse directions, its arrival end has the flat tooth at 120 ° at all each intervals, three gardens, being used for dredging the reaction tube catalyst particles builds bridge, eliminating particle bonding, wall built-up and clogging, along with drawing off of catalyst, the bed interface descends, grain sucting tube (1) also moves down thereupon, all draws off to guarantee continuously that reaction tube (3) is interior catalyst.The other end of grain sucting tube (1) links to each other with gas-solid separator (5) by inhaling grain flexible pipe (4), plays a part the guiding gas-solid and carries stream.Grain sucting tube (1) diameter d
bWith catalyst or filler particles diameter d
pRatio be d
b/ d
p〉=3.
The said concentric gas of the present invention flows into out threeway (2), and filling or draw off catalyst under the condition that not only can be used for communicating with atmosphere also is applicable under inert gas (as nitrogen) protective condition and loads or draw off catalyst or filler particles.
The said gas-solid separator of the present invention (5), be used for unloading antigravity system, there is the gas-solid flow input port its side, and there are solid particle collection unit and floss hole in the lower end, and top is that expanding reach, bottom are the contraction section of bullet, after negative-pressure air-flow or inert gas enter gas-solid separator (5) expanding reach, air velocity die-offs, and makes catalyst or filler particles not to be carried secretly, and falls into bottom the separator (5), reach the purpose of gas solid separation, also can adopt cyclone separating structure to carry out gas solid separation.
The said catalyst filling funnel of the present invention (14) is one and is marked with containing mark, transparent or local transparent, as seen the gas-solid separator at internal accelerator interface, be used for the loading catalyst system, air-flow outlet and inert gas or atmosphere input port are arranged at its top, and there is the gas-solid flow input port upper end, side, there are solid particle collection section and floss hole in the lower end, is beneficial to the quantity of gas solid separation and definite interior loading catalyst of each reaction tube (3) or filler particles.
There is the inlet/outlet and the valve (12) of an inert gas or atmosphere the top of the said catalyst container of the present invention (6), for unloading antigravity system, the valve (13) that also has an exhaust catalyst in the bottom of container (6), when the catalyst in the container (6) or filler particles are filled, open valve (13), catalyst or filling particle are discharged in the special container.
The said row of the present invention grain pipe (9) can be arbitrarily about, move left and right, in unloading antigravity system,, can change the loading catalyst system into unloading antigravity system if will arrange a grain pipe (9) and grain sucting tube (a 1) switch.
The present invention also can load or draw off simultaneously to the catalyst or the filler particles of a plurality of reaction tubes, to accelerate the process of loading, unloading catalyst.
The present invention has the following advantages.
1. the loading, unloading antigravity system is simple in structure, does not need other auxiliary equipment, the efficient height.
2. owing in the loading, unloading antigravity system, used crux equipment-grain sucting tube, therefore be easy to load and draw off the catalyst and the filler particles of various easy bridge formations, bonding, wall built-up, obstruction.
3. used vacuum suction device load is little, and equipment is little, and energy consumption is low.Because the diameter of the reaction tube in the upright multitube fixed bed reactors is all less usually, only need very little gas flow, just can produce sufficiently high air-flow linear speed, reach the requirement of entrained catalyst or filler particles.Simultaneously, because the present invention used grain sucting tube, only require near the grain sucting tube arrival end negative-pressure air-flow to reach the requirement of entrained catalyst particles, therefore, required pressure falls very low, and low to the vacuum-pumping equipment load that requires to bleed, rate of air sucked in required is little, air-extractor is little, and the described method of existing technology Br75-06251 requires the bed catalyst to flow, and height falls in required pressure, and gas flow is big, the energy consumption height is built bridge and clogging but also need auxiliary long thatch utensil to remove.
4. be applicable to the granular materials of loading and unloading large-size, as diameter d
pThe catalyst of=8～15mm, and inert filler all can successfully pack into and draw off as porcelain ball, corundum ball etc., and unlikely bridge formation.
5. use flexibly, function is many, is applicable to the multitube vertical reactor loading and unloading catalyst that reaction tube is thin and long, is specially adapted to when producing improper interruption, need be under inert gas shielding catalyst condition uses during the various fault of treatment reactor generation in service.
6. because whole operation is all carried out under negative pressure, discharge air-flow and all pass through dust filter unit, therefore, toxic dust pollutes little.
The following examples will the invention will be further described
Example 1
One upright multitubular reactor, diameter of the housing D
a=800mm wherein has 144 diameter D
RaThe reaction tube of=38 * 3.0mm, long 3400mm, requirement according to predetermined loading amount, pack into earlier height of bed 300mm, diameter of every reaction tube is the corundum ball of 10mm, and then the spherolite catalyst of pack into height of bed 2800mm, diameter d p=1.5-2.5mm, reinstall the corundum ball that height of bed 300mm diameter is 5mm, intact up to whole dresses.When originally pouring diameter by hand into and being the corundum ball of 10mm, in reaction tube, take place the bridge formation choking phenomenon have ten surplus piece, fail to reach the predetermined altitude requirement.Adopt the catalyst method of unloading of the present invention, according to device flow process shown in Figure 1, grain sucting tube is stretched into the obstruction point, start extract system, with the corundum ball sucking-off of building bridge and blocking, and then, carry out the filling of corundum ball and catalyst according to device flow process shown in Figure 2, make the filling of catalyst everything goes well with your work and finish.Used grain sucting tube is by two long 1800mm, outside diameter d
bThe metal tube of=30mm and connection tube head assemble.
Example 2
In upright multitubular reactor with example 1, adopt the method for the invention, unload dead catalyst and filler particles according to device flow process shown in Figure 1.Grain sucting tube is extend in the reaction tube, direct reach the bed interface, start pumped vacuum systems, at first sucking-off d
pThe porcelain ball of=5mm, and be collected in the gas-solid separator, when the porcelain ball exhausts, stop to bleed, the porcelain ball is discharged in the container (6), to collect then in the special container, next time is stand-by.Bleeding regulating gas speed continues to be inserted into the dead catalyst interface with grain sucting tube, at this moment d
pThe dead catalyst of=1.5-2.5mm draws off smoothly, any bridge formation choking phenomenon do not occur, when dead catalyst exhausts, stops to bleed, and dead catalyst is emitted in the container (6), is collected in then in the dead catalyst special container, and is last, according to same step, with d
pThe porcelain ball of=10mm all draws off, and so repeats, and draws off 144 catalyst and filler particles in the reaction tube one by one, and all catalyst dusts capture in cloth envelop collector.
Example 3
A upright multitubular reactor of forming by 56 reaction tubes, the diameter D of every reaction tube
Ra=38 * 3.0mm, long 3400mm, earlier according to device flow process loading catalyst shown in Figure 2 and filler particles, carry out aminating reaction, after having reacted, adopt the grain sucting tube composite set of 8 double triangle arrangement to draw off dead catalyst and filler particles, draw off the filler particles (d that is contained in the upper strata of 300mm height earlier
p=5.0mm), draw off the catalyst granules (d of stage casing 2800mm height then
p=2.0mm), the diameter that draws off the 300mm of lower floor height at last is the filler particles of 10mm, adopts the pumped vacuum systems with example 1, and dead catalyst and filler particles are all drawn off, and the process of drawing off is accelerated greatly.
Claims (7)
1. the unloading method of the catalyst in the upright multitube fixed bed reactors, it is characterized in that adopting by grain sucting tube (1) and unload antigravity system for what critical piece was formed, draw off catalyst according to following operating procedure: the arrival end of grain sucting tube (1) is passed concentric gas flow into out threeway (2) and insert in the reaction tube (3), direct reach the bed interface of catalyst, open with concentric gas and flow into out the valve (11) that threeway (2) links to each other, start vacuum suction device (8), negative-pressure air-flow by (8) generation, by the annular space between reaction tube (3) and the grain sucting tube (1) to the catalyst bed bed boundary, the bleeding regulating air velocity, make negative-pressure air-flow carry catalyst granules secretly and go into gas-solid separator (5) through inhaling grain flexible pipe (4), meticulous catalyst dust is overflowed through the bleeding point at gas-solid separator (5) top, capture intermittently through dust filter unit (7) again and take out, catalyst granules is collected in the bottom of gas-solid separator (5), open the valve (10) of (5) bottom and the valve (12) of catalyst container (6) top, catalyst is managed (9) intermittent discharge to catalyst container (6) through row's grain.
2. according to the said catalyst method that draws off of claim 1, it is characterized in that and under inert gas shielding, to unload catalyst, in unloading antigravity system, flow into out the valve (11) that threeway (2) links to each other with concentric gas and directly link to each other with inert gas source.
3. the packing method of a upright multitube fixed bed reactor catalyst, it is characterized in that adopting the loading catalyst system that forms for critical piece by grain sucting tube (1), according to following operating procedure loading catalyst: open and inhale grain flexible pipe (4) and catalyst and load valve (16) between the funnel (14), close valve (17) below (14) and the valve (18) above (14) side and with the top of (14), gas flows into out threeway (2) with one heart, the valve (19) that dust filter unit (7) links to each other, grain sucting tube (1) insertion is equipped with in the container (6) of catalyst, direct reach catalyst interface, open the valve (12) of (6) top, start vacuum suction device (8), the bleeding regulating air velocity, the negative-pressure air-flow that (8) are produced is being carried catalyst granules secretly and is being entered catalyst filling funnel (14) through a grain sucting tube (1) and a suction grain flexible pipe (4), meticulous catalyst dust is overflowed from the top bleeding point of (14), capture intermittently taking-up through dust filter unit (7), when the quantity of the catalyst in the catalyst filling funnel (14) reaches predetermined value, stop to bleed, open valve (18,19), make system recover normal pressure, valve-off (16), open valve (17), catalyst in the catalyst filling funnel (14) passes concentric gas through dress agent pipe (15) and flows into out threeway (2) and put into reaction tube (3) lentamente.
4. according to the method for the said loading catalyst of claim 3; it is characterized in that can be at loading catalyst under the inert gas shielding, and the valve (18) of the valve (12) of catalyst container in the loading catalyst system (6) top, catalyst filling funnel (14) side top directly links to each other with inert gas source.
5. according to claim 1,3 said loading, unloading catalyst methods, it is characterized in that catalyst grain size≤15mm, also can load and unload the inert filler of same granularity.
6. according to claim 1,3 said loading, unloading catalyst methods, it is characterized in that in the loading, unloading antigravity system, between each parts, is to connect by rubber components sealing or pipeline.
7. claim 1, the 3 said critical piece grain sucting tubes (1) that are used for loading or unloading antigravity system is characterized in that the caliber d of grain sucting tube (1)
bCaliber (D less than reaction tube (3)
Ra), its length is than the long 5-10% of reaction tube (3), and the arrival end of grain sucting tube (1) has the flat tooth at 120 ° at all each intervals, three gardens, and the height of flat tooth (h) is about grain sucting tube (1) diameter d
b1/3rd, grain sucting tube (1) diameter d
bWith the catalyst diameter d
pRatio be d
b/ d
p〉=3.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN95107485A CN1049368C (en) | 1995-07-14 | 1995-07-14 | Handling method for fixed bed reactor catalyst and its main equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN95107485A CN1049368C (en) | 1995-07-14 | 1995-07-14 | Handling method for fixed bed reactor catalyst and its main equipment |
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| Publication Number | Publication Date |
|---|---|
| CN1140628A true CN1140628A (en) | 1997-01-22 |
| CN1049368C CN1049368C (en) | 2000-02-16 |
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ID=5076338
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN95107485A Expired - Fee Related CN1049368C (en) | 1995-07-14 | 1995-07-14 | Handling method for fixed bed reactor catalyst and its main equipment |
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| CN112934121A (en) * | 2021-05-14 | 2021-06-11 | 东营威联化学有限公司 | Catalyst collector fixing device for continuous reforming reactor |
| CN112934121B (en) * | 2021-05-14 | 2021-07-30 | 东营威联化学有限公司 | Catalyst collector fixing device for continuous reforming reactor |
| CN113521957A (en) * | 2021-07-19 | 2021-10-22 | 华电智控（北京）技术有限公司 | Filling method and filling device for VOCs-enriched adsorption tube |
| CN113521957B (en) * | 2021-07-19 | 2023-02-28 | 华电智控（北京）技术有限公司 | Filling method and filling device for VOCs-enriched adsorption tube |
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