Coal hydrogenation pyrolysis and gasification coupled method
Technical field
The present invention relates to a kind of coal resources comprehensive utilization technique, relate in particular to a kind of coal hydrogenation pyrolysis and gasification coupled method.
Background technology
Enter 21 century, along with the rapid growth of economy, to the also sharply increase of demand of industrial chemicals, in the industrial chemicals structure, coal accounts for over half, and " development Coal Chemical Industry, exploitation and popularization clean coal technology " become the common recognition of industrial community and academia.For the classification that realizes coal resources efficiently utilizes, academia has proposed the process imagine of " coal pulls out head ", fully extracts gas, liquid fuel and fine chemicals in coal.
In the prior art, the tar yield of pyrolysis of coal technology is lower, and light constituent content is less; The quick hydropyrolysis technology of coal can improve tar yield, obtains the high heating value gas of methane rich simultaneously, but in the feed coal still some carbon exist with low value-added semicoke form, the total carbon utilisation rate of raw material is lower.Coal Gasification Technology can obtain the different synthetic gas of gaseous fraction by selecting different vaporized chemicals, but with regard to specific gasifying medium, its synthesis gas components is more single, also can't extract more valuable Coal Chemical Industry products such as naphthalene, benzene, phenol simultaneously.
Summary of the invention
The purpose of this invention is to provide a kind of coal hydrogenation pyrolysis and gasification coupled method, this method combines coal hydrogenation pyrolysis, semicoke hydrogasification and the hydrogen manufacturing of burnt grain, fully in coal, extract gas, liquid fuel and fine chemicals, combine the advantage of pyrolysis of coal technology and Coal Gasification Technology, effectively improve tar yield and light constituent content, can obtain simultaneously the Coal Chemical Industry products such as naphthalene, benzene, phenol of methane rich pyrolysis coal gas and gasification gas and high added value.
The objective of the invention is to be achieved through the following technical solutions:
Coal hydrogenation pyrolysis of the present invention and gasification coupled method comprise the processing step of following order:
A, the feed coal that granularity is less than or equal to 2mm carry out drying and preheating in coal drying and preheating system, dry back total water is less than or equal to 8%, and preheating temperature is 250-350 ℃;
Feed coal 60%-80% after drying and the preheating enters the coal hydrogenation pyrolysis oven, under pressure 1.0-3.0MPa and temperature 550-680 ℃ condition, carry out hydropyrolysis, the pyrolysis gas-phase product enters pyrolysis gas purification separation system to be separated, and the product after the separation comprises: methane rich pyrolysis coal gas, tar, naphthalene, benzene, phenol etc.;
The semicoke of B, the production of described coal hydrogenation pyrolysis oven all enters burnt hydrogasification stove, under pressure 1.0-3.0MPa and temperature 327-427 ℃ condition, carry out hydrogasification, the gasification gas-phase product enters gasification gas purification separation system, isolates the gasification gas that is rich in methane;
Feed coal 20%-40% after C, drying and the preheating with divides under the acting in conjunction of oxygen and water vapor mixture agent from the porous of described burnt hydrogasification stove, loose high-temperature coke grain about two-way enter rich hydrogen generator, under pressure 1.0-3.0MPa and temperature 900-1500 ℃ condition, carry out gasification reaction, the hydrogen-rich gas of producing uses as the fluidized reaction gas of described coal hydrogenation pyrolysis oven, and its lime-ash is handled in removing slag system and finished.
As seen from the above technical solution provided by the invention, coal hydrogenation pyrolysis that the embodiment of the invention provides and gasification coupled method, because coal hydrogenation pyrolysis, semicoke hydrogasification and the hydrogen manufacturing of burnt grain are combined, can fully in coal, extract gas, liquid fuel and fine chemicals, the advantage of comprehensive pyrolysis of coal technology and Coal Gasification Technology, effectively improve tar yield and light constituent content, can obtain simultaneously the Coal Chemical Industry products such as naphthalene, benzene, phenol of methane rich pyrolysis coal gas and gasification gas and high added value.
Description of drawings
In order to be illustrated more clearly in the technical scheme of the embodiment of the invention, the accompanying drawing of required use is done to introduce simply in will describing embodiment below, apparently, accompanying drawing in describing below only is some embodiments of the present invention, for those of ordinary skill in the art, under the prerequisite of not paying creative work, can also obtain other accompanying drawings according to these accompanying drawings.
Fig. 1 is the process flow sheet of coal hydrogenation pyrolysis of the present invention with gasification coupled method.
Among the figure: 1, coal drying and preheating system, 2, the coal hydrogenation pyrolysis oven, 3, burnt hydrogasification stove, 4, rich hydrogen generator, 5, pyrolysis gas purification separation system, 6, the gasification gas purification system, 7, remove slag system.
Embodiment
Below in conjunction with the accompanying drawing in the embodiment of the invention, the technical scheme in the embodiment of the invention is clearly and completely described, obviously, described embodiment only is the present invention's part embodiment, rather than whole embodiment.Based on embodiments of the invention, those of ordinary skills belong to protection scope of the present invention not making the every other embodiment that is obtained under the creative work prerequisite.
Coal hydrogenation pyrolysis of the present invention and gasification coupled method, its preferable embodiment comprises the processing step of following order as shown in Figure 1:
A, the feed coal that granularity is less than or equal to 2mm carry out drying and preheating in coal drying and preheating system, dry back total water is less than or equal to 8%, and preheating temperature is 250-350 ℃;
Feed coal 60%-80% after drying and the preheating enters the coal hydrogenation pyrolysis oven, under pressure 1.0-3.0MPa and temperature 550-680 ℃ condition, carry out hydropyrolysis, the pyrolysis gas-phase product enters pyrolysis gas purification separation system to be separated, and the product after the separation comprises: methane rich pyrolysis coal gas, tar, naphthalene, benzene, phenol etc.;
The semicoke of B, the production of described coal hydrogenation pyrolysis oven all enters burnt hydrogasification stove, under pressure 1.0-3.0MPa and temperature 327-427 ℃ condition, carry out hydrogasification, the gasification gas-phase product enters gasification gas purification separation system, isolates the gasification gas that is rich in methane;
Feed coal 20%-40% after C, drying and the preheating with divides under the acting in conjunction of oxygen and water vapor mixture agent from the porous of described burnt hydrogasification stove, loose high-temperature coke grain about two-way enter rich hydrogen generator, under pressure 1.0-3.0MPa and temperature 900-1500 ℃ condition, carry out gasification reaction, the hydrogen-rich gas of producing uses as the fluidized reaction gas of described coal hydrogenation pyrolysis oven, and its lime-ash is handled in removing slag system and finished.
Described coal hydrogenation pyrolysis oven is a fluidized-bed reactor, the pyrolysis coal gas after fluidized reaction gas is purified by a part and form from the hydrogen-rich gas of rich hydrogen generator;
Described burnt hydrogasification stove is a fluidized-bed reactor, and fluidized reaction gas is the pyrolysis coal gas after a part purifies;
Described rich hydrogen generator is the cyclone bed reactor.
The present invention combines coal hydrogenation pyrolysis, semicoke hydrogasification and the hydrogen manufacturing of burnt grain, fully in coal, extract gas, liquid fuel and fine chemicals, combine the advantage of pyrolysis of coal technology and Coal Gasification Technology, effectively improve tar yield and light constituent content, can obtain simultaneously the Coal Chemical Industry products such as naphthalene, benzene, phenol of methane rich pyrolysis coal gas and gasification gas and high added value.
Specific embodiment:
Industrial scale with coal treatment capacity 2t/h is an example, and the technical analysis before and after the upgrading of feed coal sees Table 1.The feed coal of mean particle size 0.6mm carries out drying and preheating in coal drying and preheating system (1) after, preheating temperature is 270 ℃, wherein 60% feed coal is introduced into coal hydrogenation pyrolysis oven (2), under pressure 1.0MPa and 600 ℃ of conditions of temperature, carry out hydropyrolysis, the pyrolysis gas-phase product enters pyrolysis gas purification separation system (5) and carries out purification separation, wherein productive rates 4% such as pyrolysis gas yield 19.68% (methane-containing gas 52%), tar yield 14.63%, naphthalene, benzene, phenol; The solid product semicoke all enters burnt hydrogasification stove (3), carries out hydrogasification under pressure 1.0 and 327 ℃ of conditions of temperature, and the gasification gas-phase product enters gasification gas purification system (6), and the gasification gas component after the purification sees Table 2; Remaining burnt the feed coal with 40% in burnt hydrogasification stove (3) gasification back divides up and down under the acting in conjunction of oxygen and water vapor mixture agent, and two-way enters rich hydrogen generator (4), further gasification reaction under pressure 1.0 and 1000 ℃ of conditions of temperature, the hydrogen-rich gas component of producing sees Table 3, and its lime-ash is handled in removing slag system (7) and finished.
Technical analysis result (%) before and after the upgrading of table 1 feed coal
Sequence number |
Title |
Ratio/% before the dehydration |
Dehydration back ratio/% |
1 |
Total water/M
t |
17.9 |
2.5 |
2 |
Empty butt moisture/M
ad |
9.45 |
|
3 |
As received basis ash content/A
ar |
9.05 |
10.75 |
4 |
As received basis fugitive constituent/V
ar |
29.40 |
34.91 |
5 |
As received basis fixed carbon/FC
ar |
43.65 |
51.84 |
|
Lower heat value/Q
net,ar |
21.35MJ/kg |
25.24MJ/kg |
The gasification gas component that table 2 hydrogasification stove is produced
Sequence number |
Chemical name |
Content % (v/v) |
1 |
Hydrogen |
28.6 |
2 |
Carbonic acid gas |
13.4 |
3 |
Carbon monoxide |
32.0 |
4 |
Methane |
26.0 |
The gaseous fraction that the rich hydrogen generator of table 3 is produced
Sequence number |
Chemical name |
Content % (v/v) |
1 |
Hydrogen |
35.0 |
2 |
Carbonic acid gas |
15.0 |
3 |
Carbon monoxide |
47.0 |
4 |
Unsaturated olefin |
2.0 |
5 |
Nitrogen |
1.0 |
The present invention compared with prior art has the following advantages:
Technical modules such as coal hydrogenation pyrolysis that (1) the present invention is integrated, semicoke hydrogasification, the hydrogen manufacturing of burnt grain, realized the effective extension of product chain and the comprehensive utilization of feed coal, also can coal hydrogenation pyrolysis, three technical modules of semicoke hydrogasification and burnt grain hydrogen manufacturing have been carried out different combinations according to the market requirement;
(2) the present invention can obtain the rich CH of high added value by the hydropyrolysis operation
4Pyrolysis coal gas can effectively improve tar yield and light constituent content simultaneously;
(3) gasification gas of hydrogasification explained hereafter of the present invention is rich in CH
4Gas can be used as instead of natural gas and uses;
(4) rich hydrogen generator of the present invention utilizes the porous that forms after coal hydrogenation pyrolysis and the hydrogasification, loose high-temperature coke grain and the mixture of part material coal to prepare hydrogen-rich gas as solid material, and reaction efficiency height, total efficiency of carbon conversion are big.
The above; only for the preferable embodiment of the present invention, but protection scope of the present invention is not limited thereto, and anyly is familiar with those skilled in the art in the technical scope that the present invention discloses; the variation that can expect easily or replacement all should be encompassed within protection scope of the present invention.Therefore, protection scope of the present invention should be as the criterion with the protection domain of claims.