CN103706308B - A kind of self-loopa combination reaction device - Google Patents
A kind of self-loopa combination reaction device Download PDFInfo
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Abstract
A kind of self-loopa combination reaction device, relates to a kind of chemosynthesis reaction device.Form primarily of reative cell, upper chamber, cooling coil, decline passway, lower chamber and shell, upper chamber is above reative cell, the below of reative cell is lower chamber, and decline passway is made up of the space between the middle housing of shell and reative cell wall body, and cooling coil is arranged in decline passway; Reative cell wall body is made up of cylinder sidewall and circular arc bottom, and reative cell wall body is connected on shell by upper supporting piece and lower support element, has circulating air input port to access and catalyst discharge outlets picks out in the lower sidewall of reative cell wall body or curved bottom; Lower chamber has raw material tonifying Qi interface to access, and the bottom of lower chamber is liquid collecting zone, and the bottom of liquid collecting zone has product exit to pick out.The present invention adopts cooling coil as the cooling device in decline passway, makes unstripped gas only just all need can synthesize target product by first compression, significantly to reduce power consumption and to improve catalytic efficiency.
Description
Technical field
The present invention relates to a kind of chemical industry equipment, be related specifically to a kind of chemosynthesis reaction device.
Background technology
Under catalyst existent condition, most of chemosynthesis reaction is all reversible reaction, after target product reaches finite concentration, will be in balance, reacts and will no longer carry out to the direction of synthesis target product.People are in the production process of carrying out combination reaction, can continue to make reaction to carry out to target product direction, mix products must be made to export from synthesis reactor and fill into new raw material gas in synthesis reactor, target product concentration in synthesis reactor is reduced, combination reaction is made to proceed after destruction of balance, after mix products exports from synthesis reactor, by separation equipment, unreacting gas is separated, again unreacting gas is returned in synthesis reactor and carry out circular response, because one way catalytic rate is only about 20%, unstripped gas must by being reacted into target product after the compression that repeatedly circulates in synthesis reactor, and the compression that circulates all needs to consume very large compression energy consumption at every turn.
In existing synthesis reactor, under the condition of applications catalyst synthesis, the operating pressure of synthetic ammonia is at more than 8MPa, the operating pressure of synthesizing methanol is between 3 ~ 15MPa, the operating pressure of direct synthesis of dimethyl ether from synthesis gas is between 2 ~ 5MPa, obtain above-mentioned operating pressure, multi-stage compression must be taked to realize, compression energy consumption is very large, therefore, existing synthesis reactor repeatedly must circulate and unstripped gas could be synthesized the production process of target product with multi-stage compression, there is the shortcoming that power consumption is large.
Summary of the invention
The object of the invention is to overcome existing chemical synthesis equipment and unstripped gas need be carried out the large shortcoming of iterative cycles compression power consumption, design a kind of combination reaction device being carried out automatic cycle catalysis by synthesis reactor oneself in inside, make unstripped gas only just all need can synthesize target product by first compression, significantly to reduce power consumption and to improve catalytic efficiency, in the production of synthetic ammonia, methyl alcohol, dimethyl ether and need carry out realizing energy-saving and emission-reduction in the production process of chemical synthesis at other.
A kind of self-loopa combination reaction device of the present invention, it is characterized in that combination reaction device is primarily of reative cell (IV), upper chamber (VI), cooling coil (24), decline passway (V), lower chamber (III) and shell (9) composition, wherein, reative cell (IV), upper chamber (VI), cooling coil (24), decline passway (V) and lower chamber (III) are arranged in the interior space of shell (9), upper chamber (VI) is in the top of reative cell (IV), the below of reative cell (IV) is lower chamber (III), decline passway (V) is made up of the space between the middle housing of shell (9) and reative cell wall body (7), the interior space that upper chamber (VI) is surrounded by upper end (3) and shell (9) upper casing is formed, the interior space that lower chamber (III) is surrounded by piece housing under lower end (15) and shell (9) is formed, reative cell (IV) is communicated to upper chamber (VI), and upper chamber (VI) is communicated to lower chamber (III) by decline passway (V), reative cell wall body (7) is made up of cylinder sidewall and circular arc bottom, reative cell wall body (7) is connected on the housing of shell (9) by upper supporting piece (5) and lower support element (22), has circulating air input port (23) to access and catalyst discharge outlets (11) picks out in the lower sidewall of reative cell wall body (7) or curved bottom, cooling coil (24) is arranged in decline passway (V), the housing that the lower end of cooling coil (24) passes shell (9) hypomere is connected on cooling water inlet (21), and the housing that the upper end of cooling coil (24) passes shell (9) epimere is connected on coolant outlet (25), lower chamber (III) has raw material tonifying Qi interface (20) to access, lower chamber (III) is communicated to the bottom of reative cell (IV) by circulating air input port (23), the bottom of lower chamber (III) is liquid collecting zone (I), and the bottom of liquid collecting zone (I) has product exit (16) to pick out.
In the present invention, half partition-type structures that circulating air input port (23) are multi-through hole; The lateral wall of reative cell wall body (7) is installed heat insulation layer (8); At the bottom having heaters (10) of reative cell (IV), heater (10) is electric heater and heat exchanger one wherein; The circulating air input port (23) of reative cell there is circulating air communicating pipe (13), gas skirt (19) is set in lower chamber (III), the top of gas skirt (19) is connected on the input port of circulating air communicating pipe (13), the interior space of gas skirt (19) forms collection chamber (II), and collection chamber (II) is communicated to reative cell (IV) by circulating air communicating pipe (13); In lower chamber (III), have gas-liquid separator (14), gas-liquid separator (14) comprises louvre type separator, coil pipe cooling separator and surface cooler formula separator; The top of upper end (3) has catalyst charging hole (VII), and catalyst charging hole (VII) is closed by top cover (1), between top cover (1) and upper end (3) joint face, have sealing ring a(2); Upper end (3) is disk structure, and upper end (3) is arranged on the upper port of shell (9), between upper end (3) and the joint face of shell (9) upper port, have sealing ring b(4); Lower end (15) is circular arc bottom structure, and lower end (15) is arranged on the lower port of shell (9), has sealing ring c(18 between the lower port of shell (9) and the joint face of lower end (15)).
In foregoing invention, because reative cell (IV), upper chamber (VI), decline passway (V) and lower chamber (III) coexist in the space of shell (9), and reative cell (IV) is directly communicated to upper chamber (VI), upper chamber (VI) is directly communicated to decline passway (V), decline passway (V) is directly communicated to lower chamber (III), therefore, combination reaction device carries out self-loopa catalytic synthesis under equal pressure condition, make the wall body of reative cell (IV) (7) not bear pressure, the material usage of wall body (7) can be greatly reduced.
Foregoing invention in the specific implementation, cooling water inlet (21) is connected on the feed pipe of cooling system, coolant outlet (25) is connected on the return pipe of cooling system, catalyst is set in reative cell (IV) simultaneously, the requirement of catalyst according to target product is selected and activates, then in combination reaction device, unstripped gas is inputted, unstripped gas is made to enter in reative cell (IV), just combination reaction is carried out in reative cell (IV), generate target product, when unstripped gas carries out combination reaction, heat can be produced, the reaction heat generated can make to heat up in reative cell (IV), thus the unreacting gas in reative cell (IV) and gaseous state target product are heated up, the density of the gaseous mixture of unreacting gas and the mixing of gaseous state target product is diminished, according to gravity circulation principle, gaseous mixture after intensification can carry out ascending motion, enter into upper chamber (VI), simultaneously, decline passway (V) is subject to the cooling effect of cooling coil (24), unreacting gas in decline passway (V) or gaseous mixture are cooled, temperature declines, the density of unreacting gas or gaseous mixture is increased, according to gravity circulation principle, unreacting gas after cooling or gaseous mixture can carry out descending motion, enter into lower chamber (III), gaseous mixture in lower chamber (III) after gas-liquid separator (14) is separated, be separated into liquid target product and the unreacting gas of gaseous state, liquid target product is exported by product exit (16) and product efferent duct (17) and enters product storage tank, unreacting gas carries out circular response by circulating air communicating pipe (13) entering reative cell (IV) by circulating air input port (23), the unstripped gas that synthesis target product consumes is supplemented by raw material tonifying Qi interface (20), so go round and begin again, by combination reaction device oneself, in inside, isobaric condition forms automatic cycle, and isolate target product in time, make target product concentration in combination reaction device all the time lower than equalization point, make combination reaction can continue to carry out.The present invention makes unstripped gas only just all need can synthesize target product by first compression, and do not need a mixture output-response device to be separated outward, overcome unstripped gas and need carry out the large shortcoming of iterative cycles compression power consumption, improve catalytic efficiency, realize energy-saving and emission-reduction.
In above-mentioned invention, in reative cell wall body (7) in combination reaction device and the space between shell (9), cooling coil (24) is set, make gaseous mixture fast cooling and carry out descending motion, the downward gravitation of automatic generation, thus make the space between reative cell wall body (7) and shell (9) be subject to cooling effect and form the decline passway (V) of gaseous mixture, gaseous mixture in upper chamber (VI) is incorporated in lower chamber (III), in lower chamber (III), gaseous mixture is separated again, isolated unreacting gas supplements in reative cell (IV) by circulating air input port (23) in time, the gaseous mixture heated up in driving a reaction room (IV) accelerates ascending motion, the gaseous mixture accelerating ascending motion in reative cell (IV) makes the gaseous mixture in decline passway (V) accelerate descending motion by ringing again, thus, oneself constantly circulation power is produced in inside by combination reaction device.The present invention adopts cooling coil (24) as the cooling device in decline passway (V), cooling tube is made to be coiled in decline passway (V) equably, realize the cooling effect of decline passway (V), cooling coil (24) only needs an input interface and an output interface, therefore, at epimere and the hypomere of shell (9), respectively only have an exit points, compared with the cooling device of cooling tube bundle, eliminate diversion box and header tank, further, make simpler and save material.
In above-mentioned invention, the effect arranging heater (10) in the bottom of reative cell (IV) is for reative cell (IV) carries out auxiliary heating, the room temperature of target product synthesis is applicable in the initial generation of equipment investment operation, the adjustment of operating temperature is carried out when equipment normally runs, meanwhile, the effect making unstripped gas accelerate circulation catalysis is played.Described heater (10) is electric heater or heat exchanger, selects existing products in markets.
In above-mentioned invention, gas skirt (19) is set in lower chamber (III) and has circulating air communicating pipe (13) on circulating air input port (23), the top of gas skirt (19) is connected on the input port of circulating air communicating pipe (13), its effect is that unreacting gas is assembled at gas skirt (19), the interior space of gas skirt (19) is made to form collection chamber (II), heavy target product is made not enter the top of gas skirt (19), thus prevent the gaseous target product in lower chamber (III) from feeding back in reative cell (IV) by circulating air input port (23), be conducive to improving the catalytic efficiency in reative cell (IV).
In above-mentioned invention, gas-liquid separator (14) is set in lower chamber (III), its objective is that a target product is separated in time, reduce the target product concentration in combination reaction device, combination reaction is carried out to favourable direction, makes unstripped gas accelerate synthesis target product, improve catalytic efficiency.Described gas-liquid separator (14) comprises louvre type separator, coil pipe cooling separator and surface cooler formula separator, when using louvre type separator, gas-liquid separation is carried out to collide separate mode, when aerosol particle in mixture runs into louver plate washer in flow process, agglomerating and form liquid target product through colliding mutually condensation; When using coil pipe cooling separator and surface cooler formula separator, gas-liquid separation is carried out in condensation separation mode, when the surface temperature of coil pipe or surface cooler drops to below the evaporating temperature of target product, just the target product of gaseous state is made to condense in the surface of coil pipe or surface cooler and isolate liquid product, or when the room temperature of lower chamber (III) is reduced to below the evaporating temperature of target product, the target product of gaseous state is just condensed into liquid target product, reaches separation object.
In above-mentioned invention, circulating air input port (23) is designed to half partition-type structures of multi-through hole, catalyst in reative cell (IV) can not be leaked by circulating air input port (23), and half partition-type structures of multi-through hole can not hinder unreacting gas to enter in reative cell (IV).
In above-mentioned invention, the object that the lateral wall of the wall body (7) of reative cell is installed heat insulation layer (8) is the cooling effect making the reaction heat in reative cell (IV) can not have influence on decline passway (V), also make the cooling effect of decline passway (V) that thermogenic action in reative cell (IV) can not be had influence on simultaneously, thus ensure the temperature that keeps chemical reaction to need in reative cell (IV).
The invention has the beneficial effects as follows: a kind of self-loopa combination reaction device of design, adopt cooling coil as the cooling device in decline passway, when guaranteeing the cooling effect realizing decline passway, making structure simpler, reducing material usage; During production, make unstripped gas only just all need can synthesize target product by first compression, significantly to reduce power consumption and to improve catalytic efficiency, in the production process of chemical synthesis, realize energy-saving and emission-reduction.Compared with routine techniques, instant invention overcomes conventional chemical synthesis equipment need carry out the large shortcoming of iterative cycles compression power consumption unstripped gas.The present invention can apply on the production line of the chemical synthesis products such as methyl alcohol, dimethyl ether, synthetic ammonia.
Accompanying drawing explanation
Accompanying drawing is the structure chart of a kind of self-loopa combination reaction device of the present invention.
In figure: 1. top cover, 2. sealing ring a, 3. upper end, 4. sealing ring b, 5. upper supporting piece, 6. temperature sensor, 7. reative cell wall body, 8. heat insulation layer, 9. shell, 10. heater, 11. catalyst discharge outlets, 12. catalyst discharge ducts, 13. circulating air communicating pipes, 14. gas-liquid separators, 15. lower ends, 16. product exit, 17. product efferent ducts, 18. sealing ring c, 19. gas skirts, 20. raw material tonifying Qi interfaces, 21. cooling water inlets, 22. lower support elements, 23. circulating air input ports, 24. cooling coils, 25. coolant outlets, I. liquid collecting zone, II. collection chamber, III. lower chamber, IV. reative cell, V. decline passway, VI. upper chamber, VII. catalyst charging hole.
Detailed description of the invention
In embodiment shown in the drawings, self-loopa combination reaction device is primarily of reative cell (IV), upper chamber (VI), cooling coil (24), decline passway (V), lower chamber (III) and shell (9) composition, wherein, reative cell (IV), upper chamber (VI), cooling coil (24), decline passway (V) and lower chamber (III) are arranged in the interior space of shell (9), upper chamber (VI) is in the top of reative cell (IV), the below of reative cell (IV) is lower chamber (III), decline passway (V) is made up of the space between the middle housing of shell (9) and reative cell wall body (7), the interior space that upper chamber (VI) is surrounded by upper end (3) and shell (9) upper casing is formed, the interior space that lower chamber (III) is surrounded by piece housing under lower end (15) and shell (9) is formed, reative cell (IV) is communicated to upper chamber (VI), and upper chamber (VI) is communicated to lower chamber (III) by decline passway (V), reative cell wall body (7) is made up of cylinder sidewall and circular arc bottom, reative cell wall body (7) is connected on the housing of shell (9) by upper supporting piece (5) and lower support element (22), has circulating air input port (23) access and catalyst discharge outlets (11) to pick out at the curved bottom of reative cell wall body (7), cooling coil (24) is arranged in decline passway (V), the housing that the lower end of cooling coil (24) passes shell (9) hypomere is connected on cooling water inlet (21), and the housing that the upper end of cooling coil (24) passes shell (9) epimere is connected on coolant outlet (25), lower chamber (III) has raw material tonifying Qi interface (20) to access, lower chamber (III) is communicated to the bottom of reative cell (IV) by circulating air input port (23), the bottom of lower chamber (III) is liquid collecting zone (I), and the bottom of liquid collecting zone (I) has product exit (16) to pick out.In the present embodiment, half partition-type structures that circulating air input port (23) are multi-through hole; The lateral wall of reative cell wall body (7) is installed heat insulation layer (8); At the bottom having heaters (10) of reative cell (IV), heater (10) is electric heater, selects commercially available prod; The circulating air input port (23) of reative cell there is circulating air communicating pipe (13), gas skirt (19) is set in lower chamber (III), the top of gas skirt (19) is connected on the input port of circulating air communicating pipe (13), the interior space of gas skirt (19) forms collection chamber (II), and collection chamber (II) is communicated to reative cell (IV) by circulating air communicating pipe (13); In lower chamber (III), have gas-liquid separator (14), gas-liquid separator (14) is coil pipe cooling separator, selects commercially available prod; The top of upper end (3) has catalyst charging hole (VII), and catalyst charging hole (VII) is closed by top cover (1), between top cover (1) and upper end (3) joint face, have sealing ring a(2); Upper end (3) is disk structure, and upper end (3) is arranged on the upper port of shell (9), between upper end (3) and the joint face of shell (9) upper port, have sealing ring b(4); Lower end (15) is circular arc bottom structure, and lower end (15) is arranged on the lower port of shell (9), has sealing ring c(18 between the lower port of shell (9) and the joint face of lower end (15)); Temperature sensor (6) is had in upper chamber (VI).
When the present embodiment is applied on producing, cooling water inlet (21) is connected on the feed pipe of cooling system, coolant outlet (25) is connected on the return pipe of cooling system, catalyst is set in reative cell (IV) simultaneously, the requirement of catalyst according to target product is selected and activates, then in combination reaction device, unstripped gas is inputted, unstripped gas is made to enter in reative cell (IV), just combination reaction is carried out in reative cell (IV), generate target product, when unstripped gas carries out combination reaction, heat can be produced, the reaction heat generated can make to heat up in reative cell (IV), thus the unreacting gas in reative cell (IV) and gaseous state target product are heated up, the density of the gaseous mixture of unreacting gas and the mixing of gaseous state target product is diminished, according to gravity circulation principle, gaseous mixture after intensification can carry out ascending motion, enter into upper chamber (VI), simultaneously, decline passway (V) is subject to the cooling effect of cooling coil (24), unreacting gas in decline passway (V) or gaseous mixture are cooled, temperature declines, the density of unreacting gas or gaseous mixture is increased, according to gravity circulation principle, unreacting gas after cooling or gaseous mixture can carry out descending motion, enter into lower chamber (III), gaseous mixture in lower chamber (III) after gas-liquid separator (14) is separated, be separated into liquid target product and the unreacting gas of gaseous state, liquid target product is exported by product exit (16) and product efferent duct (17) and enters product storage tank, unreacting gas carries out circular response by circulating air communicating pipe (13) entering reative cell (IV) by circulating air input port (23), the unstripped gas that synthesis target product consumes is supplemented by raw material tonifying Qi interface (20), so go round and begin again, by combination reaction device oneself, in inside, isobaric condition forms automatic cycle, and isolate target product in time, make target product concentration in combination reaction device all the time lower than equalization point, make combination reaction can continue to carry out.The present invention makes unstripped gas only just all need can synthesize target product by first compression, and do not need a mixture output-response device to be separated outward, overcome unstripped gas and need carry out the large shortcoming of iterative cycles compression power consumption, improve catalytic efficiency, realize energy-saving and emission-reduction.In process of production, obtain the temperature in reative cell (IV) by temperature sensor (6), then by the temperature that operate heater (10) is run or stopping controls in reative cell (IV), make it the temperature requirement meeting chemical synthesis.
The production line of the above embodiments as methyl alcohol, dimethyl ether, synthetic ammonia or other chemical synthesis product is applied.When applying as synthesizing methanol equipment, arrange at reative cell (IV) with the Al of the CuO of 48%, the ZnO of 46% and 5%
2o
3for the pellet type catalyst of component, then the H of the CO of a volume and two volumes
2be input in combination reaction device as unstripped gas after mixing, carry out synthesizing methanol production, the reaction equation that unstripped gas synthesizes methyl alcohol is CO+2H
2→ CH
3oH+102.5kj; When applying as one-step synthesis method dimethyl ether equipment, arrange at reative cell (IV) with the Al of the CuO of 48%, the ZnO of 46% and 5%
2o
3for the pellet type catalyst of component, then add and fill out ZSM-5 molecular sieve, then the H of the CO of a volume and two volumes
2be input in combination reaction device as unstripped gas after mixing, carry out dimethyl ether synthesis production, the reaction equation that unstripped gas synthesizes dimethyl ether is 2CO+4H
2→ (CH
3)
2o+H
2o+200.2kj; When applying as ammonia synthesis unit, arrange with catalyst component based on Fe, with Al at reative cell (IV)
2o
3, K
2o, CaO, SiO
2, BaO is promoter, then the N of a volume
2with the H of three volumes
2be input in combination reaction device as unstripped gas after mixing, carry out Ammonia Production, the reaction equation that unstripped gas synthesizes ammonia is N
2+ 3H
2→ 2NH
3+ 92.1kj.
Claims (9)
1. a self-loopa combination reaction device, it is characterized in that combination reaction device is primarily of reative cell (IV), upper chamber (VI), cooling coil (24), decline passway (V), lower chamber (III) and shell (9) composition, wherein, reative cell (IV), upper chamber (VI), cooling coil (24), decline passway (V) and lower chamber (III) are arranged in the interior space of shell (9), upper chamber (VI) is in the top of reative cell (IV), the below of reative cell (IV) is lower chamber (III), decline passway (V) is made up of the space between the middle housing of shell (9) and reative cell wall body (7), the interior space that upper chamber (VI) is surrounded by upper end (3) and shell (9) upper casing is formed, the interior space that lower chamber (III) is surrounded by piece housing under lower end (15) and shell (9) is formed, reative cell (IV) is communicated to upper chamber (VI), and upper chamber (VI) is communicated to lower chamber (III) by decline passway (V),
Reative cell wall body (7) is made up of cylinder sidewall and circular arc bottom, reative cell wall body (7) is connected on the housing of shell (9) by upper supporting piece (5) and lower support element (22), has circulating air input port (23) to access and catalyst discharge outlets (11) picks out in the lower sidewall of reative cell wall body (7) or curved bottom; Cooling coil (24) is arranged in decline passway (V), the housing that the lower end of cooling coil (24) passes shell (9) hypomere is connected on cooling water inlet (21), and the housing that the upper end of cooling coil (24) passes shell (9) epimere is connected on coolant outlet (25); Lower chamber (III) has raw material tonifying Qi interface (20) to access, lower chamber (III) is communicated to the bottom of reative cell (IV) by circulating air input port (23), the bottom of lower chamber (III) is liquid collecting zone (I), and the bottom of liquid collecting zone (I) has product exit (16) to pick out.
2. a kind of self-loopa combination reaction device according to claim 1, is characterized in that half partition-type structures that circulating air input port (23) is multi-through hole.
3. a kind of self-loopa combination reaction device according to claim 1, is characterized in that on the lateral wall of reative cell wall body (7), install heat insulation layer (8).
4. a kind of self-loopa combination reaction device according to claim 1, is characterized in that the bottom having heaters (10) at reative cell (IV), and heater (10) is electric heater and heat exchanger one wherein.
5. a kind of self-loopa combination reaction device according to claim 1, it is characterized in that there is circulating air communicating pipe (13) on the circulating air input port (23) of reative cell, gas skirt (19) is set in lower chamber (III), the top of gas skirt (19) is connected on the input port of circulating air communicating pipe (13), the interior space of gas skirt (19) forms collection chamber (II), and collection chamber (II) is communicated to reative cell (IV) by circulating air communicating pipe (13).
6. a kind of self-loopa combination reaction device according to claim 1, is characterized in that there is gas-liquid separator (14) in lower chamber (III), and gas-liquid separator (14) comprises louvre type separator, coil pipe cooling separator and surface cooler formula separator.
7. a kind of self-loopa combination reaction device according to claim 1, it is characterized in that on the top of upper end (3), have catalyst charging hole (VII), catalyst charging hole (VII) is closed by top cover (1), between top cover (1) and upper end (3) joint face, have sealing ring a(2).
8. a kind of self-loopa combination reaction device according to claim 1, it is characterized in that upper end (3) is disk structure, upper end (3) is arranged on the upper port of shell (9), between upper end (3) and the joint face of shell (9) upper port, have sealing ring b(4).
9. a kind of self-loopa combination reaction device according to claim 1, it is characterized in that lower end (15) is for circular arc bottom structure, lower end (15) is arranged on the lower port of shell (9), has sealing ring c(18 between the lower port of shell (9) and the joint face of lower end (15)).
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5143698A (en) * | 1990-03-05 | 1992-09-01 | Uop | Apparatus for internal backmix cooling |
| CN101143729A (en) * | 2007-09-05 | 2008-03-19 | 湖南安淳高新技术有限公司 | Multi-bed layer shaft radial synthesizing tower |
| CN201135882Y (en) * | 2007-10-29 | 2008-10-22 | 沈建冲 | Axis radial direction low resistance synthesis reactor |
| CN203591782U (en) * | 2013-12-16 | 2014-05-14 | 衢州昀睿工业设计有限公司 | Self-circulation chemical combination reactor |
-
2013
- 2013-12-16 CN CN201310682627.5A patent/CN103706308B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5143698A (en) * | 1990-03-05 | 1992-09-01 | Uop | Apparatus for internal backmix cooling |
| CN101143729A (en) * | 2007-09-05 | 2008-03-19 | 湖南安淳高新技术有限公司 | Multi-bed layer shaft radial synthesizing tower |
| CN201135882Y (en) * | 2007-10-29 | 2008-10-22 | 沈建冲 | Axis radial direction low resistance synthesis reactor |
| CN203591782U (en) * | 2013-12-16 | 2014-05-14 | 衢州昀睿工业设计有限公司 | Self-circulation chemical combination reactor |
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