CN208883486U - Schizolysis hydrogen production plant with methanol - Google Patents
Schizolysis hydrogen production plant with methanol Download PDFInfo
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- CN208883486U CN208883486U CN201821329670.8U CN201821329670U CN208883486U CN 208883486 U CN208883486 U CN 208883486U CN 201821329670 U CN201821329670 U CN 201821329670U CN 208883486 U CN208883486 U CN 208883486U
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- furnace
- pyrolysis furnace
- hydrogen production
- production plant
- input duct
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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The utility model discloses schizolysis hydrogen production plant with methanol, including gasification furnace, consistencyregulator, gasification furnace connects material liquid pipeline, concentration ratio adjuster is fixedly mounted on material liquid pipeline, metering pump is provided on gasification furnace, gasification furnace is connected on pyrolysis furnace by input duct, concentration detector is provided in input duct, concentration detector relative position is provided with nitrogen pressurizer, input duct tube head position extends in cushion chamber, cushion chamber is located at cracking furnace bottom, liner is equipped in pyrolysis furnace, reaction chamber is equipped in liner, reaction chamber is communicated with cushion chamber, pyrolysis furnace is externally provided with circulating pump, circulating pump passes through pyrolysis furnace and is connected with reaction chamber, pyrolysis furnace is equipped with escape pipe, adsorption tower is connected on escape pipe.Rationally, structure is simple for the utility model design, promotes convenient for a wide range of.
Description
Technical field
The utility model relates to industrial technical fields, in particular to schizolysis hydrogen production plant with methanol.
Background technique
Existing methanol hydrogen production equipment, when gasification furnace is reacted into reactor, be primarily due to insufficient pressure or
Catalyst bridging seriously or in reactor has hollow pipeline, and buckling is slow, causes methanol decomposition speed slow, and cracking is incomplete,
Secondly, the concentration of material liquid will constantly follow up when methanol decomposition, concentration is small, and cracking is insufficient, and material liquid contacts less with catalyst,
Waste of resource, purification amount is few, is specifically designed a kind of methanol decomposition hydrogen manufacturing equipment thus, and material liquid can be made full use of to carry out hydrogen manufacturing and mentioned
It is pure.
Utility model content
The purpose of this utility model is to provide hydrogen production from coal gasification device, which enters gasification furnace
Concentration, reactor is carried out after being preheated, the control of concentration ensure that and sufficiently merge when methanol decomposition with catalyst, improve
Rate of cleavage does not waste raw material.
The purpose of this utility model is achieved by following technical proposals: schizolysis hydrogen production plant with methanol, including gasification
Furnace, consistencyregulator, gasification furnace are connected to material liquid pipeline, concentration ratio adjuster, gas are fixedly mounted on material liquid pipeline
Change and be provided with metering pump on furnace, gasification furnace is connected on pyrolysis furnace by input duct, and Concentration Testing is provided in input duct
Device is provided with nitrogen pressurizer with concentration detector relative position, and input duct tube head position extends in cushion chamber, cushion chamber
Positioned at cracking furnace bottom, it is equipped with liner in pyrolysis furnace, is equipped with reaction chamber in liner, reaction chamber is communicated with cushion chamber, outside pyrolysis furnace
Equipped with circulating pump, circulating pump passes through pyrolysis furnace and is connected with reaction chamber, and pyrolysis furnace is equipped with escape pipe, is connected to inhale on escape pipe
Attached tower.
As a kind of perferred technical scheme: concentration ratio adjuster is divided into two, and one is concentration of raw material ratio tune
Device is saved, one is high steam concentration ratio adjuster.
As a kind of perferred technical scheme: the inner wall aperture of input duct tube head position.
As a kind of perferred technical scheme: outlet pipe outer wall is equipped with cooling chamber.
As a kind of perferred technical scheme: adsorption tower is provided with multiple.
Compared with prior art, the utility model has the beneficial effects that the new structure can improve methanol on the whole
The effective percentage of cracking, while catalyst can be made full use of to realize cracking, together according to the concentration of control material liquid when reaction hydrogen manufacturing
When the novel upper setting circulating pump can occur building bridge in mixing to avoid catalyst or when material liquid carries out reactor, instead
It answers device hollow open circuit occur, influences lytic effect.
Detailed description of the invention
Fig. 1 is the utility model overall schematic.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment, based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, fall within the protection scope of the utility model.
As shown in Figure 1, schizolysis hydrogen production plant with methanol, including gasification furnace 1, consistencyregulator 2, gasification furnace 1 are connected to raw material
Liquid pipe road 12 is fixedly mounted concentration ratio adjuster 2 on material liquid pipeline 12, metering pump 3 is provided on gasification furnace 1, gasifies
Furnace 1 is connected on pyrolysis furnace 6 by input duct 13, concentration detector 4 is provided in input duct 13, with concentration detector 4
Relative position is provided with nitrogen pressurizer 5, and 13 tube head position of input duct extends in cushion chamber 8, and cushion chamber 8 is located at pyrolysis furnace
6 bottoms, pyrolysis furnace 6 is interior to be equipped with liner 7, is equipped with reaction chamber 14 in liner 7, reaction chamber 14 is communicated with cushion chamber 8, outside pyrolysis furnace 6
Equipped with circulating pump 9, circulating pump 9 passes through pyrolysis furnace 6 and is connected with reaction chamber 14, and pyrolysis furnace 6 is equipped with escape pipe 10, escape pipe 10
On be connected to adsorption tower 11.
In the present embodiment, it is two that concentration ratio adjuster 2, which is divided to, and one is concentration of raw material proportional controller, one
It is high steam concentration ratio adjuster.
In the present embodiment, 13 tube head position inner wall aperture of input duct.
In the present embodiment, 10 outer wall of escape pipe is equipped with cooling chamber.
In the present embodiment, adsorption tower 11 is provided with multiple.
Specifically, the utility model passes through the concentration and high steam and oxygen that concentration ratio adjuster adjusts material liquid when in use
The carry out concentration of gas, material liquid enter reactor by gasification furnace preheating, the entrance pressure of methanol can be improved by metering pump,
Accelerate cracking, while guaranteeing that methanol feeds stability, the circulating pump on pyrolysis furnace can dredge catalyst, avoid urging
Agent and methanol occur building bridge when acting on or the hollow situation of open circuit, nitrogen pressurizer can carry out pipeline when in use
Air displacement, adsorption tower setting is multiple, carries out adsorption recovery according to different gas is decomposed.
It is obvious to a person skilled in the art that the present invention is not limited to the details of the above exemplary embodiments, and
And without departing substantially from the spirit or essential attributes of the utility model, it can realize that this is practical new in other specific forms
Type.Therefore, in all respects, the present embodiments are to be considered as illustrative and not restrictive, this is practical new
The range of type is indicated by the appended claims rather than the foregoing description, it is intended that containing for the equivalent requirements of the claims will be fallen in
All changes in justice and range are embraced therein.It should not treat any reference in the claims as limiting
Related claim.
In addition, it should be understood that although this specification is described in terms of embodiments, but not each embodiment is only wrapped
Containing an independent technical solution, this description of the specification is merely for the sake of clarity, and those skilled in the art should
It considers the specification as a whole, the technical solutions in the various embodiments may also be suitably combined, forms those skilled in the art
The other embodiments being understood that.
Claims (5)
1. schizolysis hydrogen production plant with methanol, including gasification furnace (1), concentration ratio adjuster (2), it is characterised in that: gasification furnace (1) is even
Then material liquid pipeline (12) are fixedly mounted concentration ratio adjuster (2) on material liquid pipeline (12), and gasification furnace is set on (1)
It is equipped with metering pump (3), gasification furnace (1) is connected on pyrolysis furnace (6) by input duct (13), and input duct is provided on (13)
Concentration detector (4) is provided with nitrogen pressurizer (5) with concentration detector (4) relative position, input duct (13) tube head position
It extends in cushion chamber (8), cushion chamber (8) is located at pyrolysis furnace (6) bottom, liner (7) is equipped in pyrolysis furnace (6), in liner (7)
Equipped with reaction chamber (14), reaction chamber (14) is communicated with cushion chamber (8), and pyrolysis furnace (6) is externally provided with circulating pump (9), and circulating pump (9) is worn
It crosses pyrolysis furnace (6) to be connected with reaction chamber (14), pyrolysis furnace (6) is equipped with escape pipe (10), and escape pipe is connected to inhale on (10)
Attached tower (11).
2. schizolysis hydrogen production plant with methanol according to claim 1, it is characterised in that: concentration ratio adjuster (2) is divided into two
A, one is concentration of raw material proportional controller, and one is high steam concentration ratio adjuster.
3. schizolysis hydrogen production plant with methanol according to claim 1, it is characterised in that: input duct (13) tube head position inner wall
Aperture.
4. schizolysis hydrogen production plant with methanol according to claim 1, it is characterised in that: escape pipe (10) outer wall is equipped with cooling
Chamber.
5. schizolysis hydrogen production plant with methanol according to claim 1, it is characterised in that: adsorption tower (11) is provided with multiple.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821329670.8U CN208883486U (en) | 2018-08-17 | 2018-08-17 | Schizolysis hydrogen production plant with methanol |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821329670.8U CN208883486U (en) | 2018-08-17 | 2018-08-17 | Schizolysis hydrogen production plant with methanol |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208883486U true CN208883486U (en) | 2019-05-21 |
Family
ID=66509090
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821329670.8U Active CN208883486U (en) | 2018-08-17 | 2018-08-17 | Schizolysis hydrogen production plant with methanol |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208883486U (en) |
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2018
- 2018-08-17 CN CN201821329670.8U patent/CN208883486U/en active Active
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