CN205528742U - System for utilize straw blasting to prepare marsh gas - Google Patents
System for utilize straw blasting to prepare marsh gas Download PDFInfo
- Publication number
- CN205528742U CN205528742U CN201620088999.4U CN201620088999U CN205528742U CN 205528742 U CN205528742 U CN 205528742U CN 201620088999 U CN201620088999 U CN 201620088999U CN 205528742 U CN205528742 U CN 205528742U
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- CN
- China
- Prior art keywords
- biogas
- explosion
- preparing pool
- cstr reactor
- marsh gas
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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- Processing Of Solid Wastes (AREA)
Abstract
The utility model discloses a system for utilize straw blasting to prepare marsh gas, including steam explosion tank, steam explosion tank is connected with the allotment pond, and the allotment pond is connected with the screw pump, and the screw pump is connected with the CSTR reactor, and the CSTR reactor is connected with marsh gas purifier, and marsh gas purifier is connected with the finished product gas holder, and the finished product gas holder is connected with power generation facility, and power generation facility is respectively with steam explosion tank with allocate the pond and be connected. This system is that marsh gas new technic is produced to the straw of a low energy consumption, low running cost, has thoroughly solved high, the with high costs problem of straw pretreatment energy consumption, and its social and economic benefits are showing.
Description
Technical field
The utility model belongs to biogas Preparation equipment technical field, is specifically related to a kind of system utilizing stalk explosion Biogas.
Background technology
Along with fast development and the adjustment of rural energy structure of China's economy, crop residue is no longer the whole of life of farmers fuel, and the agricultural wastes of excess, how particularly stalk processes, and has become as the burden of peasant and government in recent years.A very long time in past, peasant utilizes the method for burning, is gone back fertile in field, but DeGrain, this not only wastes biomass resource, and environment be also result in pollution, in the specific period, communications and transportation and aviation safety is constituted great threat.Therefore, in fossil energy day by day deficient, today of energy form growing tension, the mankind start sight focuses on newborn energy field, and in many new forms of energy, biomass energy is considered as the energy the safest, most stable of.
China is one of agricultural production state maximum in the world, the annual all kinds of crop materials about 6-7 hundred million tons produced, comprehensive utilization makes good use of the green resource of this preciousness, advance stalk recovery energy, it is possible not only to realization turn waste into wealth, reduce environmental pollution, promotion Energy restructuring, increase farmers' income, and develop a circular economy especially, propulsion energy-saving reduces discharging, it is achieved the Important Action of low-carbon economy.
Biogas as a kind of high-efficiency cleaning energy it has been recognised that, but the biogas engineering with stalk as primary raw material is little, this is relevant with the composition of stalk and architectural characteristic, stalk is mainly cellulose, hemicellulose and lignin composition, stick to each other and be interrupted mutually, this structure is unfavorable for the anaerobic bacteria utilization to cellulose, need to pre-process it, just can apply to biomass energy source domain.And present stage, pretreatment to cellulose substances mainly has Physical, chemical method, physical-chemical process and bioanalysis, various methods emphasize particularly on different fields and pros and cons, and for anaerobic bacteria, the broken and degraded of cellulose, hemicellulose and lignin is the key factor of factor of created gase and gas production.
Steam blasting is a kind of method to cellulose substances pretreatment.Stalk is under high temperature, high steam effect, and cellulose crystallity improves, and the degree of polymerization declines, hemicellulose fraction is degraded, lignin softens, and horizontal strength of connection declines, and even softens plastic, when the material sudden pressure reduction of full steam, out of breath acute expansion in hole, produces " explosion " effect, can be partially stripped lignin, and by raw material tear for fiber fines, it is especially advantageous for hydrolyzing the contact degraded aerogenesis of bacterium and anaerobic bacteria.But certain energy can be consumed during carrying out explosion, for this, this process system, in line with the principle of cascaded utilization of energy, makes energy consumption reach to maximally utilize from links such as production technology, energy-consuming, utilizations of waste as resource, demonstrates significant economic benefit and environmental benefit.
Utility model content
For straw utilization problem present in prior art, the utility model provides the system of a kind of stalk explosion Biogas, alleviates environmental pollution, it is achieved biomass energy clean utilization.
For solve above-mentioned technical problem, the utility model by the following technical solutions:
A kind of system utilizing stalk explosion Biogas, including steam-explosion jar, described steam-explosion jar is connected with preparing pool, preparing pool is connected with screw pump, screw pump is connected with CSTR reactor, and CSTR reactor is connected with methane purifying device, and methane purifying device is connected with finished product gas holder, finished product gas holder is connected with TRT, and TRT is connected with steam-explosion jar and preparing pool respectively.
Described CSTR reactor is connected with solid-liquid separator, and solid-liquid separator is connected with preparing pool.
Described methane purifying device includes that digester and drain sump, CSTR reactor are connected with drain sump, and drain sump is connected with digester, and digester is connected with finished product gas holder.
Described preparing pool is connected with roots blower by pipeline, and preparing pool is arranged over biogas slurry return tank.
The beneficial effects of the utility model are: dry method explosion, power consumption is less, the dwell time is short, production efficiency is high, equipment Operating Management is convenient, and material flow is short, in material, waste heat loss is little, energy can recycle by step, the biogas direct generation of electricity of generation, and generating waste-heat can be as the quick-fried power of stalk vapour；Stalk after biogas slurry after separation of solid and liquid is the most quick-fried with vapour mixes, and makes the waste heat of biogas slurry have also been obtained and maximally utilizes.Through Air Exposure, in raw material, be i.e. passed through the air (aeration) of trace, side can obvious oxidative lignin, the most not only can further make the separation of lignin and cellulose, and can decompose and lignin degrading, gas production and factor of created gase can be increased substantially；Therefore, native system be a kind of low energy consumption, low operating cost stalk produce biogas novel process, thoroughly solve the problem that stalk pretreatment energy consumption is high, cost is high, its Social benefit and economic benefit is notable.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
As shown in Figure 1, a kind of system utilizing stalk explosion Biogas, including steam-explosion jar 1, described steam-explosion jar 1 is connected with preparing pool 3, preparing pool 3 is connected with screw pump 4, screw pump 4 is connected with CSTR reactor 5, CSTR reactor 5 is connected with methane purifying device, methane purifying device includes drain sump 6 and digester 7, CSTR reactor 5 is connected with drain sump 6, and drain sump 6 is connected with digester 7, and digester 7 is connected with finished product gas holder 8, finished product gas holder 8 is connected with TRT 9, and TRT 9 is connected with steam-explosion jar 1 and preparing pool 3 respectively.
CSTR reactor 5 is connected with solid-liquid separator 10, and solid-liquid separator 10 is connected with preparing pool 3；Described preparing pool 3 is connected with roots blower 11 by pipeline, and preparing pool 3 is arranged over biogas slurry return tank 2.
Working effect of the present utility model is as follows:
Stalk meal is broken to 20-30mm, delivers into steam-explosion jar, be added without any material, carry out dry method vapour quick-fried；The quick-fried state modulator of vapour: saturated vapour pressure is 1.8-2.0MPa and 2.0-2.2MPa, the tank body dwell time is 3.5-4 minute and 3.0-3.5 minute；
Stalk after vapour is quick-fried mixes with biogas slurry (device adds water before starting), solid-to-liquid ratio is 1:5, enter preparing pool, then utilize roots blower to be passed through air, carry out being interrupted aeration (30 minutes+20 minutes), time 4-6 hour, then squeeze into CSTR reactor 5 via screw pump 4 to react, biogas slurry and biogas residue carries out separation of solid and liquid by solid-liquid separator 10, and it is fertile that biogas residue does organic biogas residue, and biogas slurry is all back to preparing pool 3 and recycles；The biogas that CSTR reactor 5 produces stores to finished product gas holder after purifying further via drain sump 6 and digester 7, waste heat for generating steam after generating electricity via TRT 9, steam enters steam-explosion jar 1, as the power that stalk vapour is quick-fried, after generating, waste water is used for heating material in preparing pool 3, it is achieved energy cascade circulates.
Native system be a kind of low energy consumption, low operating cost stalk produce biogas novel process, thoroughly solve stalk and produce the problem that biogas degraded is difficult, its Social benefit and economic benefit is notable, beneficially industrial applications.
Of the present utility model general principle and principal character and of the present utility model advantage have more than been shown and described.Skilled person will appreciate that of the industry; the utility model is not restricted to the described embodiments; described in above-described embodiment and specification, principle of the present utility model is simply described; on the premise of without departing from the utility model spirit and scope; the utility model also has various changes and modifications, in the range of these changes and improvements both fall within claimed the utility model.The utility model claims scope and is defined by appending claims and equivalent thereof.
Claims (4)
1. the system utilizing stalk explosion Biogas, including steam-explosion jar (1), it is characterized in that: described steam-explosion jar (1) is connected with preparing pool (3), preparing pool (3) is connected with screw pump (4), screw pump (4) is connected with CSTR reactor (5), CSTR reactor (5) is connected with methane purifying device, methane purifying device is connected with finished product gas holder (8), finished product gas holder (8) is connected with TRT (9), and TRT (9) is connected with steam-explosion jar (1) and preparing pool (3) respectively.
The system utilizing stalk explosion Biogas the most according to claim 1, it is characterised in that: described CSTR reactor (5) is connected with solid-liquid separator (10), and solid-liquid separator (10) is connected with preparing pool (3).
The system utilizing stalk explosion Biogas the most according to claim 1, it is characterized in that: described methane purifying device includes drain sump (6) and digester (7), CSTR reactor (5) is connected with drain sump (6), drain sump (6) is connected with digester (7), and digester (7) is connected with finished product gas holder (8).
The system utilizing stalk explosion Biogas the most according to claim 1, it is characterised in that: described preparing pool (3) is connected with roots blower (11) by pipeline, and preparing pool (3) is arranged over biogas slurry return tank (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620088999.4U CN205528742U (en) | 2016-01-29 | 2016-01-29 | System for utilize straw blasting to prepare marsh gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620088999.4U CN205528742U (en) | 2016-01-29 | 2016-01-29 | System for utilize straw blasting to prepare marsh gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205528742U true CN205528742U (en) | 2016-08-31 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620088999.4U Expired - Fee Related CN205528742U (en) | 2016-01-29 | 2016-01-29 | System for utilize straw blasting to prepare marsh gas |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205528742U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116769568A (en) * | 2023-06-05 | 2023-09-19 | 中国华电科工集团有限公司 | Straw treatment system and method |
-
2016
- 2016-01-29 CN CN201620088999.4U patent/CN205528742U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116769568A (en) * | 2023-06-05 | 2023-09-19 | 中国华电科工集团有限公司 | Straw treatment system and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160831 Termination date: 20180129 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |