CN210122559U

CN210122559U - Thermal power plant pyrolysis hydrogen production system

Info

Publication number: CN210122559U
Application number: CN201920348772.2U
Authority: CN
Inventors: 陈辉; 杨豫森; 崔华
Original assignee: Hep Energy And Environment Technology Co ltd
Current assignee: HEPP Energy Environment Technology Co.,Ltd.
Priority date: 2019-03-19
Filing date: 2019-03-19
Publication date: 2020-03-03
Anticipated expiration: 2029-03-19

Abstract

The utility model discloses a thermal power plant's pyrolysis hydrogen manufacturing system, including power boiler, steam turbine and generator equipment, still include: the system comprises a feeding part, a gasification furnace, a gas purification and separation device, a high-temperature flue gas lead-out pipe and a waste gas return pipe, wherein the gasification furnace is used for pyrolyzing any one of coal, biomass, garbage and sludge fuel into pyrolysis mixed gas rich in hydrogen; the gas purification and separation device purifies and separates the mixed gas to obtain hydrogen; the power station boiler furnace is provided with a high-temperature flue gas lead-out pipe, the high-temperature flue gas lead-out pipe is connected with the gasification furnace, the gasification furnace is connected with a gas purification and separation device, and purified and separated waste gas is connected and discharged into the power station boiler furnace or a flue through a waste gas return pipe.

Description

Thermal power plant pyrolysis hydrogen production system

Technical Field

The utility model belongs to pyrolysis gasification hydrogen manufacturing field specifically is to utilize power station boiler flue gas or vapor pyrolysis coal, living beings, rubbish or mud hydrogen manufacturing.

Background

Hydrogen is currently recognized as the cleanest fuel and also a very important chemical feedstock. Therefore, hydrogen will become a very important clean energy source in the 21 st century. At present, high attention is paid to the development of hydrogen production technology in all countries in the world. In general, hydrogen production techniques can be divided into two broad categories: (1) hydrogen is produced by water electrolysis; (2) the hydrogen is produced by converting other primary energy sources, mainly fossil energy sources (coal, petroleum and natural gas) are used as raw materials to be subjected to conversion reaction with water vapor at high temperature, carbon in the fossil energy is firstly changed into CO, and then the CO is converted into CO2 and H2O is converted into hydrogen through CO conversion (namely water gas conversion) reaction.

The conversion of hydrogen from other primary energy sources, such as pyrolysis gasification of coal and renewable energy fuels, is an important source of hydrogen in the future. The prior art has a supercritical water fluidized bed reactor, and improves utility model in domestic patent 201610570395.8 to a hydrogen production device and method by supercritical water gasification of coal with recycled raffinate, but the supercritical water gasification device has high temperature and high pressure, and the device itself consumes energy greatly. The domestic patent 201610152324.6 discloses a method for preparing hydrogen-rich gas by synchronously gasifying biomass pyrolysis gas and biomass charcoal gas, the temperature of the gas-solid synchronous gasification reaction of the gasification device is 700-.

How to reduce the energy consumption of high-temperature water vapor and other working media in the hydrogen production process by pyrolysis and gasification becomes a problem to be solved urgently.

Disclosure of Invention

An object of the utility model is to provide a pyrolysis hydrogen manufacturing system of thermal power plant, with coal, living beings, rubbish or mud pyrolysis gasification for combustible pyrolysis gas mixture, again through purifying and separating to realize thermal power plant's pyrolysis hydrogen manufacturing technology.

Specifically, the utility model discloses a realize through following technical scheme:

the utility model provides a thermal power plant's pyrolysis hydrogen manufacturing system, includes power boiler, steam turbine and generator equipment, still includes: pan feeding portion, gasifier, gaseous purification and separator, high temperature flue gas eduction tube and waste gas back flow, wherein:

the gasification furnace is used for pyrolyzing any one of coal, biomass, garbage and sludge fuel into pyrolysis mixed gas rich in hydrogen;

the gas purification and separation device purifies and separates the mixed gas to obtain hydrogen;

the power station boiler furnace is provided with a high-temperature flue gas lead-out pipe, the high-temperature flue gas lead-out pipe is connected with the gasification furnace, the gasification furnace is connected with a gas purification and separation device, and purified and separated waste gas is connected and discharged into the power station boiler furnace or a flue through a waste gas return pipe.

Preferably, the gasification furnace comprises a catalyst adding port, and the catalyst is selected correspondingly according to the type of the fuel fed into the gasification furnace.

Preferably, the gasification furnace comprises a water vapor introducing pipe, and the water vapor introducing pipe introduces part of main steam or extracted steam of a steam turbine of the thermal power plant into the gasification furnace.

Preferably, the gasification furnace can adopt an oxygen-enriched gasification technology, oxygen-enriched gas is used as a gasification agent and is introduced into the gasification furnace, and the gas production rate of the gasification furnace and the hydrogen production rate of mixed gas are improved.

Preferably, the hydrogen obtained by purification and separation by the gas purification and separation device is sent to a hydrogen storage tank or a hydrogen pipeline for external delivery, and is sold externally in the form of bottled gas, a prying tank truck or pipeline gas.

Preferably, the exhaust gas obtained by purification and separation by the gas purification and separation device is returned to any position in front of a reheater, a economizer, an air preheater and a denitration device of a flue of the power station boiler according to the temperature of the exhaust gas.

Preferably, the gasification furnace comprises a coal, biomass, garbage or sludge feeding port, a slag discharging port and a pyrolysis mixed gas outlet, and the pyrolysis mixed gas outlet is connected with a gas purifying and separating device gas supply pipeline.

The utility model has the advantages that:

(1) the high-temperature flue gas of the power station boiler is used as a gasifying agent, so that the waste heat of the flue gas is efficiently utilized, and the energy consumption of the gasification furnace is reduced.

(2) High-temperature extracted steam of a steam turbine of a thermal power plant is used as a gasifying agent, waste heat of extracted steam and a steam working medium are efficiently utilized, the energy consumption of the gasification furnace is reduced, and the hydrogen yield is improved.

(3) Coal powder produced by a coal mill and a coal pulverizing system of a thermal power plant is directly utilized to carry out coal powder pyrolysis hydrogen production.

(4) The boiler flue gas or the steam extracted by the steam turbine is used for drying biomass, garbage or sludge, so that the energy consumption of the whole pyrolysis process is reduced.

Drawings

In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to these drawings without creative efforts.

Fig. 1 is a schematic structural diagram of a thermal power plant pyrolysis hydrogen production system provided in an embodiment of the present invention;

fig. 2 is a specific schematic diagram of a thermal power plant pyrolysis hydrogen production system provided in an embodiment of the present invention;

FIG. 3 is a schematic flow chart of a hydrogen production method of a thermal power plant pyrolysis hydrogen production system according to an embodiment of the present invention;

FIG. 4 is a schematic flow chart of a hydrogen production method using a thermal power plant pyrolysis hydrogen production system provided in the second embodiment of the present invention;

FIG. 5 is a schematic flow chart of a hydrogen production method using a thermal power plant pyrolysis hydrogen production system provided by the third embodiment of the present invention;

FIG. 6 is a schematic flow chart of a hydrogen production method using a thermal power plant pyrolysis hydrogen production system provided by the fourth embodiment of the present invention;

fig. 7 is a schematic structural diagram of a thermal power plant pyrolysis hydrogen production system according to a sixth embodiment of the present invention;

fig. 8 is a schematic structural diagram of a thermal power plant pyrolysis hydrogen production system according to a seventh embodiment of the present invention;

fig. 9 is a schematic structural diagram of a thermal power plant pyrolysis hydrogen production system according to an eighth embodiment of the present invention;

fig. 10 is a schematic structural diagram of a thermal power plant pyrolysis hydrogen production system according to a ninth embodiment of the present invention;

fig. 11 is a schematic structural diagram of a thermal power plant pyrolysis hydrogen production system provided in the tenth embodiment of the present invention;

fig. 12 is a schematic structural diagram of a thermal power plant pyrolysis hydrogen production system according to an eleventh embodiment of the present invention;

fig. 13 is a schematic structural diagram of a thermal power plant pyrolysis hydrogen production system according to a twelfth embodiment of the present invention;

fig. 14 is a schematic structural diagram of a thermal power plant pyrolysis hydrogen production system according to a thirteenth embodiment of the present invention;

fig. 15 is a schematic structural diagram of a thermal power plant pyrolysis hydrogen production system according to a fourteenth embodiment of the present invention;

fig. 16 is a schematic structural diagram of a thermal power plant pyrolysis hydrogen production system according to a fifteenth embodiment of the present invention;

fig. 17 is a schematic structural diagram of a thermal power plant pyrolysis hydrogen production system according to a sixteenth embodiment of the present invention;

fig. 18 is a schematic structural view of a thermal power plant pyrolysis hydrogen production system provided by a seventeenth embodiment of the present invention.

Description of the reference numerals

For further clarity of explanation of the structure and connections between the various components of the present invention, the following reference numerals are given and described.

A utility boiler 10; an exhaust gas discharge port 101; an exhaust gas treatment device 102; a flue gas treatment device 1021; an air preheater 1022; activated carbon adsorption device 1023; a dust collector 1024; a valve 11; a feeding part 12; a refuse storage pit 1 a; a grab bucket 1 b; a percolate pond 1 c; a gasification furnace 1; a drying device 11'; a pyrolysis gasification chamber 12'; a secondary combustion chamber 13'; a gas purification and separation device 8; a biomass extract container 81; a hot water tank 82; a heating network 83; a gas boiler 84; a feed inlet 14; a slag discharge port 15; a dryer 16; a cooler 2; a steam drum 3; a superheater 4; a steam turbine 5; an economizer 6; a boiler flue 7.

Through the above reference sign explanation, combine the embodiment of the utility model, can more clearly understand and explain the technical scheme of the utility model.

Detailed Description

Reference will now be made in detail to the exemplary embodiments, examples of which are illustrated in the accompanying drawings. When the following description refers to the accompanying drawings, like numbers in different drawings represent the same or similar elements unless otherwise indicated. The embodiments described in the following exemplary embodiments do not represent all embodiments consistent with the present invention. Rather, they are merely examples of apparatus and methods consistent with certain aspects of the invention, as detailed in the appended claims.

The terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the invention. As used in this specification and the appended claims, the singular forms "a", "an", and "the" are intended to include the plural forms as well, unless the context clearly indicates otherwise. It should also be understood that the term "and/or" as used herein refers to and encompasses any and all possible combinations of one or more of the associated listed items.

It is to be understood that although the terms first, second, third, etc. may be used herein to describe various information, such information should not be limited to these terms. These terms are only used to distinguish one type of information from another. For example, the first information may also be referred to as second information, and similarly, the second information may also be referred to as first information, without departing from the scope of the present invention. The word "if" as used herein may be interpreted as "at … …" or "when … …" or "in response to a determination", depending on the context.

The present invention will be described in detail below by way of examples.

Example one

A thermal power plant pyrolysis hydrogen production system, as shown in fig. 1, includes a utility boiler 10, a steam turbine and a generator device, and further includes: the device comprises a feeding part 12, a gasification furnace 1, a gas purification and separation device 8, a high-temperature flue gas eduction tube and a waste gas return tube, wherein the upper end of the gasification furnace 1 is provided with a feeding hole 14, and the lower end is provided with a slag discharge hole 15; the feeding part 12 is connected with the feeding hole 14, the gasification furnace 1 is connected with the power station boiler 10 and the gas purifying and separating device 8, and the gasification purifying and separating device 8 is connected with the power station boiler 10, that is, the power station boiler 10, the gasification furnace 1 and the gasification purifying and separating device 8 are sequentially connected end to form a circulating system. Part of high-temperature flue gas in the power station boiler 10 is conveyed to the gasification furnace 1 through a pipeline; a valve 11 is arranged between the utility boiler 10 and the gasification furnace 1, and the delivery quantity of the high-temperature flue gas delivered to the gasification furnace 1 from the utility boiler 10 can be effectively controlled by controlling the valve 11. The mixed gas generated in the gasification furnace 1 is conveyed to the gasification purification and separation device 8 through a pipeline, hydrogen is obtained through purification and separation of the gasification purification and separation device 8, and the rest of the waste gas is conveyed to the power station boiler 10, and the power station boiler 10 performs waste heat utilization.

The gasification furnace 1 is used for pyrolyzing any one pyrolysis material of coal, biomass, garbage and sludge fuel into pyrolysis mixed gas rich in hydrogen; the gas purification and separation device 8 purifies and separates the mixed gas to obtain hydrogen. The pyrolysis material is conveyed to the gasification furnace 1 through the feeding port 14, and the residue generated by the gasification furnace 1 is discharged through the slag discharging port 15.

The high-temperature flue gas extraction pipe is arranged on a hearth of the power station boiler 10 and is connected with the gasification furnace 1, the gasification furnace 1 is connected with the gas purification and separation device 8, and the waste gas purified and separated by the gas purification and separation device 8 is connected with a waste gas return pipe and is discharged into the hearth or a flue of the power station boiler 10. The gasification furnace 1 comprises a catalyst adding port, and the catalyst is selected correspondingly according to the type of the fuel fed into the gasification furnace 1. The gasification furnace 1 includes a steam introduction pipe that introduces main steam or extraction steam of a part of the steam turbine into the gasification furnace 1. As shown in fig. 2, the gasification furnace 1 is connected to a steam turbine 5 of a thermal power plant, and the water vapor in the gasification agent is from main steam or extraction steam in the steam turbine 5. The high-temperature main steam or extracted steam of a steam turbine of a thermal power plant is used as a gasifying agent, the waste heat of the main steam or extracted steam and the steam working medium are efficiently utilized, the energy consumption of the gasification furnace is reduced, and the hydrogen production is improved.

The gasification furnace 1 can adopt an oxygen-enriched gasification technology, oxygen-enriched gas is used as a gasification agent and is introduced into the gasification furnace 1, and the gas yield of the gasification furnace 1 and the hydrogen yield of mixed gas are improved. The gasifying agent is at least one of air, oxygen, water vapor and high-temperature flue gas. Specifically, the air is preheated air. The high-temperature flue gas in the gasification agent is from the high-temperature flue gas of a boiler of a thermal power plant. The high-temperature flue gas of the power station boiler is used as a gasifying agent, so that the waste heat of the flue gas is efficiently utilized, and the energy consumption of the gasification furnace is reduced.

Low-pressure low-temperature extracted steam from a steam turbine 5 of a thermal power plant is introduced into a high-temperature gas outlet area of the gasification furnace 1, and the low-temperature steam is used for chilling.

The hydrogen obtained by purification and separation of the gas purification and separation device 8 is sent into a hydrogen storage tank or a hydrogen pipeline for external delivery, and is sold externally in the form of bottled gas, a prying tank truck or pipeline gas.

The heat-engine plant is provided with a boiler flue 7 and comprises an economizer 6, a reheater, an air preheater and a denitration device.

Specifically, the exhaust gas purified and separated by the gas purification and separation device 8 is returned to the front side of one of the reheater, the economizer 6, the air preheater and the denitration device in the boiler flue 7 according to the temperature of the exhaust gas, so as to treat or recycle the exhaust gas. The waste gas separated by the gas purification and separation device 8 is directly discharged into a power station boiler, and the waste gas of pyrolysis gasification is treated by using a boiler flue gas treatment system, so that the waste gas and flue gas treatment cost of a gasification furnace is reduced. The gasifier comprises a coal, biomass, garbage or sludge feed inlet, a slag discharge port and a pyrolysis mixed gas outlet, wherein the pyrolysis mixed gas outlet is connected with a gas purifying and separating device gas supply pipeline.

Specifically, as shown in fig. 2, the thermal power plant pyrolysis coal gas hydrogen production system comprises a cooler 2, wherein one end of the cooler 2 is connected with a gasification furnace 1, and the other end of the cooler 2 is connected with a power station boiler 10; the mixed gas generated in the gasification furnace 1 enters a cooler 2, and the medium in the cooler 2 is boiler water of a thermal power plant. In the cooler 2, the medium boiler water in the cooler 2 absorbs the heat of the mixed gas generated by the gasification furnace 1, so that the mixed gas generated by the gasification furnace 1 is cooled, and the boiler water absorbs the heat of the mixed gas to form steam, thereby effectively surplus heat and reducing heat loss.

The cooler 2 is connected with a steam drum 3, one end of the steam drum 3 is connected with the cooler 2, and the other end of the steam drum 3 is connected with a steam turbine 5; a superheater 4 is arranged between the steam drum 3 and the steam turbine 5. The medium in the cooler 2 is formed into steam by the heat of the mixed gas generated by the gasification furnace 1, and is formed into superheated steam after passing through the superheater 4, and the superheated steam is delivered to the steam turbine 5 to be used as a power source of the steam turbine 5. The cooler 2 can effectively recover waste heat to generate steam, and the steam is converged into a boiler drum or a steam-water circulation thermodynamic system of a power plant.

Specifically, a catalyst adding port is formed in the gasification furnace 1, and the catalyst is selected according to the type of the pyrolysis material fed into the gasification furnace 1.

A thermal power plant pyrolysis hydrogen production method, as shown in fig. 3, using the thermal power plant pyrolysis hydrogen production system described in the first embodiment, the method includes the following specific implementation steps:

s1: selecting pyrolysis fuel fed into a gasification furnace according to the conditions of peripheral and regional resources of the thermal power plant, and if the pyrolysis fuel is coal, jumping to S2; if biomass, garbage or sludge, it goes to S3.

S2: according to the type of the pyrolysis raw material coal, a coal gasification process is selected, any one of a fixed bed gasification technology, a fluidized bed gasification technology and an entrained flow gasification technology can be adopted, and a gasification agent can adopt any one or any two or three of flue gas, air, oxygen and water vapor, and then the step S4 is carried out.

S3: different gasification processes are selected according to the fuel type of the pyrolysis raw material biomass, garbage or sludge, any one of a fixed bed gasification furnace, a fluidized bed gasification furnace or a rotating bed gasification furnace can be adopted, and a gasification agent can adopt any one or any two or three of flue gas, air, oxygen and water vapor, and then the mixture enters S4.

S4: pretreating the pyrolysis raw material, and processing coal into any one of particles, coal dust and coal water slurry according to the type of a gasification furnace; and crushing and drying the biomass, the garbage or the sludge.

S5: and (4) sending the pretreated pyrolysis raw material into a gasification furnace.

S6: according to the gasification process, any one or any two or three of flue gas, air, oxygen and water vapor are combined into any gasification agent and sent into the gasification furnace.

S7: the generated mixed gas is sent to a gas purification and separation device for purification treatment.

S8: and separating the purified gas to obtain hydrogen.

S9: and the residual waste gas is separated and sent to a boiler flue.

Furthermore, the pyrolysis raw material coal can be pulverized coal which directly comes from a coal mill and a coal pulverizing system of a thermal power plant.

Further, flue gas or steam in the pretreatment drying process of the pyrolysis raw material biomass, garbage or sludge comes from power station boiler flue gas or steam turbine high-temperature steam.

Example two

A coal pyrolysis gas hydrogen production system of a thermal power plant comprises a gasification furnace 1, wherein the upper end of the gasification furnace 1 is provided with a feed inlet 14, and the lower end of the gasification furnace 1 is provided with a slag discharge port 15; the pan feeding portion 12 that 14 departments of feed inlet are connected is power boiler powder process system, power boiler powder process system includes thermal power plant's coal pulverizer and powder process system, produces the buggy through thermal power plant's coal pulverizer and powder process system. The powder making system of the utility boiler conveys the prepared coal powder to the gasification furnace 1 through the feed inlet 14, and the residue generated by the gasification furnace 1 is discharged through the slag discharge port 15. Coal raw materials are pretreated in the boiler powder preparation system 12 of the station, namely, the coal pyrolysis gas hydrogen production system of the thermal power plant directly utilizes coal powder produced by a coal mill of the thermal power plant and the powder preparation system to carry out coal powder pyrolysis hydrogen production, and equipment and coal powder of the thermal power plant can be effectively utilized. Preferably, the pulverized coal produced by the powder making system of the utility boiler is pressurized and conveyed into the gasification furnace 1 by nitrogen or CO 2.

A method for producing hydrogen from coal pyrolysis gas in a thermal power plant, as shown in fig. 4, comprising the following steps:

s1': selecting a gasification process according to the type of coal and the granularity of pulverized coal of a thermal power plant; and determining the gasifying agent corresponding to the corresponding gasifying process;

s2': feeding coal powder and corresponding gasifying agent into a gasification furnace, and carrying out coal gasification reaction to obtain mixed gas;

the control system of the gasification furnace controls the amount of the coal powder sent into the gasification furnace and controls the flow and the temperature of the gasification agent sent into the gasification furnace, so that the gasification reaction energy balance equation of the gasification furnace is satisfied, and the stable gasification reaction temperature is realized.

S3': sending the generated mixed gas into a gas purification and separation device for purification treatment; separating the purified gas to obtain hydrogen; and the residual waste gas is separated and sent to a boiler flue.

EXAMPLE III

The principle of this embodiment is the same as that of the second embodiment, and the main difference is as follows: the source of the gasified pyrolysis feed is coal water slurry, not coal fines as in example one.

A method for producing hydrogen from coal pyrolysis gas in a thermal power plant, as shown in fig. 5, which comprises the following steps:

s1': selecting a gasification process according to the coal amount and the coal water slurry concentration processed by a low-speed coal mill of a thermal power plant; and determining the gasifying agent corresponding to the corresponding gasifying process;

s2': feeding the coal water slurry and a corresponding gasifying agent into a gasification furnace, and carrying out coal gasification reaction to obtain mixed gas;

the gasification furnace control system controls the amount of the water-coal slurry sent into the gasification furnace and controls the flow and the temperature of the gasification agent sent into the gasification furnace so as to meet the gasification reaction energy balance equation of the gasification furnace and realize stable gasification reaction temperature.

Example four

The principle of this embodiment is the same as that of the second embodiment, and the difference is that: the sources of the gasified pyrolysis material are coal water slurry and coal powder, but the coal powder is only used in the first embodiment. Namely, in the embodiment, the first embodiment and the second embodiment are combined into a set of coal pyrolysis gas hydrogen production system of the thermal power plant.

A method for producing hydrogen from coal pyrolysis gas in a thermal power plant, as shown in fig. 6, which comprises the following steps:

s1 ' ' ': selecting the state of the coal raw material fed into the gasification furnace according to the existing equipment of the thermal power plant and the condition of a flue gas and steam thermodynamic system; if it is pulverized coal, S2 ' ' '; if the coal water slurry is the coal water slurry, S3 '' '' is executed.

S2 ' ' ': selecting a gasification process according to the type of coal processed by a coal mill of a thermal power plant and the granularity of pulverized coal; and determining the gasifying agent corresponding to the corresponding gasifying process; then S4 ' ' '.

S3 ' ' ': selecting a gasification process according to the coal amount and the coal water slurry concentration processed by a low-speed coal mill of a thermal power plant; and determining the gasifying agent corresponding to the corresponding gasifying process; then S4 ' ' '.

S4 ' ' ': and (3) feeding the pretreated coal raw material and a corresponding gasification agent into a gasification furnace, and carrying out coal gasification reaction to obtain mixed gas.

The control system of the gasification furnace controls the amount of the coal raw material sent into the gasification furnace and controls the flow and the temperature of the gasification agent sent into the gasification furnace so as to meet the gasification reaction energy balance equation of the gasification furnace and realize stable gasification reaction temperature.

S5 ' ' ': sending the generated mixed gas into a gas purification and separation device for purification treatment; separating the purified gas to obtain hydrogen; and the residual waste gas is separated and sent to a boiler flue.

The embodiment of the utility model provides an have following advantage (1) utilize power plant boiler high temperature flue gas as the gasification agent, the high efficiency has utilized the flue gas waste heat, reduces the gasifier energy consumption. (2) High-temperature extracted steam of a steam turbine of a thermal power plant is used as a gasifying agent, waste heat of extracted steam and a steam working medium are efficiently utilized, the energy consumption of the gasification furnace is reduced, and the hydrogen yield is improved. (3) Coal powder produced by a coal mill and a coal pulverizing system of a thermal power plant is directly utilized to carry out coal powder pyrolysis hydrogen production. (4) Coal, additive and water are mixed in a coal mill to produce the coal water slurry by directly utilizing a low-speed steel ball coal mill of a thermal power plant. (5) The waste gas separated by the gas purification and separation device is directly discharged into a power station boiler, and the pyrolysis gasification waste gas is treated by using a boiler flue gas treatment system, so that the waste gas treatment cost of the gasification furnace is reduced.

EXAMPLE five

The pyrolysis material source gasified by the coal pyrolysis gas hydrogen production system of the thermal power plant is biomass. When the pyrolysis fuel fed from the feed port 14 of the gasification furnace 1 is biomass, the biomass is pyrolyzed and gasified by the gasification furnace 1 to form biomass char, biomass combustible gas, hot water, and hydrogen, the gas purification and separation device 8 separates the hydrogen, and the remaining waste gas is fed into the utility boiler 10 through the waste gas return pipe, and simultaneously, the biomass char is generated in the slag discharge port 15 of the gasification furnace 1. Further, the biomass charcoal can be made into industrial charcoal, domestic charcoal, activated charcoal, culture medium, soil improvement repairing agent, fertilizer slow release agent and the like.

EXAMPLE six

As shown in fig. 7, on the basis of the fifth embodiment, the system for producing hydrogen from coal pyrolysis gas of a thermal power plant further includes a biomass extracting solution container 81, and the biomass extracting solution container 81 is connected to the gas purifying and separating device 8; the gas purification and separation apparatus 8 is capable of separating and extracting a biomass extract from an output from the mixed gas outlet of the gasification furnace 1 and introducing the biomass extract into the biomass extract container 81. Further, the biomass extracting solution can be prepared into foliar fertilizer, disinfectant, deodorant and the like.

EXAMPLE seven

As shown in fig. 8, on the basis of the sixth embodiment, the system for producing hydrogen from pyrolysis of coal gas in a thermal power plant further includes a hot water tank 82 and a heat supply network 83, the hot water tank 82 is connected to a pipeline at the outlet of the mixed gas on the one hand, and is connected to the gas purification and separation device 8 on the other hand, the hot water separated by the gas purification and separation device 8 can be input into the hot water tank 82, and the hot water discharged from the outlet of the mixed gas can also be input into the hot water tank 82; the hot water tank 82 is also connected to a heating network 83, and is used for supplying hot water to the heating network 83 to realize heating.

Example eight

As shown in fig. 9, on the basis of the seventh embodiment, the system for producing hydrogen from coal pyrolysis gas in a thermal power plant further includes a gas boiler 84, the gas boiler 84 is connected to a waste gas return pipe, and biomass combustible gas in the waste gas return pipe enters the gas boiler 84 to be combusted, so as to generate steam for other uses.

Example nine

As shown in fig. 10, on the basis of the first embodiment, the feeding part 12 of the coal pyrolysis gas hydrogen production system of the thermal power plant is a garbage storage pit 1a, and the garbage storage pit 1a is used for storing garbage, so that the garbage is stacked and percolated in the garbage storage pit; the coal pyrolysis gas hydrogen production system of the thermal power plant further comprises a grab bucket 1b, the grab bucket 1b grabs and conveys the garbage in the garbage storage pit 1a to a feed inlet 14 of the gasification furnace 1, the gasification furnace 1 carries out pyrolysis gasification on the garbage to generate combustible pyrolysis gas, hydrogen and waste gas, the combustible pyrolysis gas, the hydrogen and the waste gas are input into the gas purification and separation device 8, the hydrogen is separated by the gas purification and separation device 8, and the waste gas is input into the power station boiler 10. Because gasifier 1 carries out pyrolysis gasification back to rubbish, not only can generate combustible pyrolysis gas and hydrogen, still can generate a large amount of flue gases, the utility model discloses in, the flue gas of production can be introduced into gasifier 1 through the high temperature flue gas fairlead.

Example ten

As shown in fig. 11, in order to prevent the smoke from being excessively larger than the amount of smoke used in the gasification furnace 1 and the excessive smoke from polluting the air, in addition to the ninth embodiment, an exhaust gas treatment device 102 is disposed at the exhaust gas outlet 101 of the utility boiler 10, and the smoke is purified to reach the standard through the exhaust gas treatment device 102, thereby reducing the pollution to the air.

EXAMPLE eleven

As shown in fig. 12, on the basis of the tenth embodiment, the exhaust gas treatment device 102 includes a flue gas treatment device 1021, an activated carbon adsorption device 1023 and a dust remover 1024, the flue gas treatment device 1021, the activated carbon adsorption device 1023 and the dust remover 1024 are connected in sequence, and the flue gas discharged from the exhaust gas outlet 101 is purified through the flue gas treatment device 1021, the activated carbon adsorption device 1023 and the dust remover 1024 in sequence, so as to form standard exhaust gas.

Example twelve

As shown in fig. 13, in addition to the ninth embodiment, the gasification furnace 1 includes a drying device 11 ', a pyrolysis gasification chamber 12', and a second combustion chamber 13 ', and the drying device 11' is connected to the feed port 14 of the gasification furnace 1, and is configured to receive the garbage fed from the feed port 14 and dry the garbage; the drying device 11 'is connected with a pyrolysis gasification chamber 12', and the pyrolysis gasification chamber 12 'receives the dried garbage conveyed from the drying device 11' and carries out pyrolysis gasification; the pyrolysis gasification chamber 12 ' is also respectively connected with a mixed gas outlet and a secondary combustion chamber 13 ', the pyrolysis gasification chamber 12 ' conveys combustible pyrolysis gas, flue gas and hydrogen to the mixed gas outlet, and conveys the pyrolyzed substances to the secondary combustion chamber 13 ' for further combustion to generate harmless ash, and the secondary combustion chamber 13 ' is connected with a slag discharge port 15 of the gasification furnace 1 and is used for discharging the harmless ash to the slag discharge port 15; the harmless ash can be treated in a landfill mode or be comprehensively utilized.

EXAMPLE thirteen

As shown in fig. 14, in addition to the twelfth embodiment, there are provided a flue gas treatment device 1021, an activated carbon adsorption device 1023 and a dust collector 1024 as in the eleventh embodiment.

Example fourteen

As shown in fig. 15, on the basis of the thirteenth embodiment, the exhaust gas treatment device 102 further includes an air preheater 1022, and the air preheater 1022 is connected between the flue gas treatment device 1021 and the activated carbon adsorption device 1023; the air preheater 1022 is also connected to the utility boiler 10 and the secondary combustion chamber 13' respectively; the flue gas passing through the flue gas treatment device 1021 is introduced into an air preheater 1022 to generate hot air, and the hot air is introduced into the power station boiler 10 and the secondary combustion chamber 13' respectively to support combustion.

Example fifteen

As shown in fig. 16, in addition to the fourteenth embodiment, the garbage storage pit 1a is further connected to an air preheater 1022, and the negative pressure deodorizing gas generated in the garbage storage pit 1a can be introduced into the air preheater 1022 to deodorize the exhaust gas flowing through the air preheater 1022.

Example sixteen

As shown in fig. 17, in addition to the fifteenth embodiment, the system for producing hydrogen from pyrolysis of coal gas in a thermal power plant further includes a leachate tank 1c, the leachate tank 1c is connected to the refuse storage pit 1a on the one hand, and is connected to the utility boiler 10 on the other hand, the refuse is stacked and percolated in the refuse storage pit to generate leachate, the leachate flows into the leachate tank 1c, the leachate in the leachate tank 1c is introduced into the utility boiler 1, and the leachate is subjected to high-temperature combustion harmless treatment.

Example seventeen

As shown in fig. 18, the system for producing hydrogen from coal pyrolysis gas of a thermal power plant comprises a gasification furnace 1, wherein a feed inlet 14 is formed in the upper end of the gasification furnace 1, and a slag discharge outlet 15 is formed in the lower end of the gasification furnace; the feed inlet 14 of gasifier 1 connects desicator 16, desicator 16 connects pan feeding portion 12, pan feeding portion 12 is arranged in carrying mud to desicator 16, desicator 16 is arranged in receiving mud pyrolysis material, desicator 16 still receives in flue gas, the high temperature steam one or the combination of these two, and the mud in flue gas, the high temperature steam or the combination of both and the desicator acts on, dries mud, and the mud after the drying is carried to gasifier 1 through feed inlet 14, and the residue that produces through gasifier 1 is discharged by row cinder notch 15.

The sludge is dried by using flue gas and high-temperature steam in the dryer, namely, the thermal power plant coal pyrolysis gas hydrogen production system directly utilizes the flue gas generated by the power generation of the existing power station boiler and the steam generated by the steam turbine to dry the sludge, then the dried sludge is conveyed to the gasification furnace 1 to carry out pyrolysis hydrogen production, and the equipment and the steam turbine which generate the flue gas of the thermal power plant can be effectively utilized.

The above description is only a preferred embodiment of the present invention, and should not be taken as limiting the invention, and any modifications, equivalent replacements, improvements, etc. made within the spirit and principle of the present invention should be included in the protection scope of the present invention.

Claims

1. The utility model provides a thermal power plant's pyrolysis hydrogen manufacturing system, includes power boiler, steam turbine and generator equipment, its characterized in that still includes: pan feeding portion, gasifier, gaseous purification and separator, high temperature flue gas eduction tube and waste gas back flow, wherein:

2. The thermal power plant pyrolysis hydrogen production system according to claim 1, wherein the gasification furnace comprises a catalyst addition port, and the catalyst is selected correspondingly according to the type of fuel fed into the gasification furnace.

3. The thermal power plant pyrolysis hydrogen production system according to claim 2, wherein the gasification furnace comprises a water vapor introduction pipe, and the water vapor introduction pipe introduces part of main steam or extracted steam of a steam turbine of the thermal power plant into the gasification furnace.

4. The thermal power plant pyrolysis hydrogen production system according to claim 1, wherein the gasification furnace can adopt an oxygen-enriched gasification technology, oxygen-enriched gas is used as a gasification agent and is introduced into the gasification furnace, and the gas production rate of the gasification furnace and the hydrogen production rate of mixed gas are improved.

5. The thermal power plant pyrolysis hydrogen production system according to claim 1, wherein the hydrogen obtained by purification and separation by the gas purification and separation device is sent to a hydrogen storage tank or an externally conveyed hydrogen pipeline and sold externally in the form of bottled gas, a skid tank truck or pipeline gas.

6. The thermal power plant pyrolysis hydrogen production system according to claim 5, wherein the waste gas obtained by purification and separation by the gas purification and separation device is returned to any position of a flue reheater, an economizer, an air preheater and a denitration device of the power plant boiler according to the temperature of the waste gas.

7. The thermal power plant pyrolysis hydrogen production system according to claim 1, wherein the gasification furnace comprises a coal, biomass, garbage or sludge feed inlet and a slag discharge port, and a pyrolysis mixed gas outlet, and the pyrolysis mixed gas outlet is connected with a gas purification and separation device gas supply pipeline.