CN202430217U

CN202430217U - Reaction chamber for generation of hydrogen or mathane

Info

Publication number: CN202430217U
Application number: CN2012200010866U
Authority: CN
Inventors: 林秋裕; 黄巧云; 赖奇厚; 陈晋照
Original assignee: Feng Chia University
Current assignee: Feng Chia University
Priority date: 2012-01-04
Filing date: 2012-01-04
Publication date: 2012-09-12
Anticipated expiration: 2022-01-04

Abstract

The utility model relates to a reaction chamber for generation of hydrogen or methane, which comprises a first shell, wherein the first shell is internally provided with at least a clapboard, the clapboard is provided with a plurality of holes in a penetrating manner, and at least two container chambers are formed in the first shell and are communicated with each other. When a user injects the mixed solution blended with matrix, microorganisms, water and the like into the container chambers, the clapboard hinders the flow of the mixed solution, so that the mixed solution flows round and round in each container chamber so as to mix the matrix and the microorganisms uniformly, therefore, the matrix and the microorganisms can fully react, and the productivity of the hydrogen or methane can be improved.

Description

The reaction chamber that hydrogen or methane generate

Technical field

The utility model relates to a kind of reaction chamber structure, is meant the reaction chamber that a kind of hydrogen or methane generate especially.

Background technology

Hydrogen and methane are because itself have higher calorific value; And generally believed it to be the rising star who replaces fossil fuel; Drop into numerous resources in the technology that develops preparation hydrogen and methane so countries in the world are numerous and confused in recent years, and in numerous technologies of preparing, a kind of technology of utilizing microbial degradation method to prepare hydrogen and methane is arranged; Because the energy that expends with less to the degree of environmental disruption, so luxuriant gradually be main flow.

See also shown in Figure 1; This microbial degradation method mainly prepares through a reaction chamber; This reaction chamber mainly has a upright cell body 1 that is provided with; And vertically be provided with two dividing plates 2 in the cell body 1, and be formed with one be positioned at 2 on said dividing plate rising runner 3, and two decline runners 4 that lay respectively at rising runner 3 both sides; In addition, the corresponding rising runner in the bottom of cell body 13 places also are equipped with an inlet 5, and the top correspondence of cell body 1 a wherein decline runner 4 places also is equipped with an outlet 6; Therefore, as long as the user is earlier will be in order to the matrix of preparation hydrogen and methane, like hexose etc.; Be mixed into a mixing liquid with mikrobes such as water and anerobess; This mixing liquid is injected in the cell body 1 by inlet 5, this mixing liquid just can be flowed by the top-direction of rising runner 3 toward cell body 1, flows out cell body 1 by outlet 6 more again; The mixing liquid of part then can be through run by gravity toward said decline runner 4 simultaneously; And mobile toward the top-direction of cell body 1 with the mixing liquid that injects again by the bottom of cell body 1 by rising runner 3, so can quicken to mix this matrix and this mikrobe, make this matrix take place to degrade and generate hydrogen or methane.

Yet; Please continue again to consult shown in Figure 1 because interconnect between rising runner 3 and the said decline runner 4 and do not have any group separated, so this mixed solution is known from experience apace through rising runner 3 and said decline runner 4; And by outlet 6 outflow cell bodies 1; Cause this matrix and this mikrobe can't be in cell body 1 complete reaction, and have a strong impact on the production capacity of hydrogen or methane, the efficient that produces hydrogen or methane is reduced greatly.

The utility model content

In view of this, the purpose of the utility model is to provide a kind of production capacity that can significantly promote hydrogen or methane, produces the hydrogen of hydrogen or methane efficient or the reaction chamber that methane generates to reach enhancement.

For achieving the above object; The reaction chamber that the utility model provides a kind of hydrogen or methane to generate, the reaction chamber that said hydrogen or methane generate includes first housing of an arranged transversely, and first housing has the rear end that a front end and is oppositely arranged; Also vertically stand in first housing simultaneously and be provided with at least one dividing plate; Be equipped with most perforation on the said dividing plate, and extreme direction is formed with at least two rooms in regular turn towards said back by said front end in said first housing, said room is connected; And first housing also is equipped with an inlet at said front position place; And inlet is connected with the room of contiguous said front end, and first housing also is equipped with an outlet at said back-end location place, and outlet is connected with the room of contiguous said rear end.

As preferred version; The reaction chamber that wherein said hydrogen or methane generate further includes at least one reflux unit; It has a reflux pump, and reflux pump is connected with a pumping pipe, and the other end of pumping pipe is communicated in a wherein room of said first housing; Reflux pump also is connected with a drain pipe simultaneously, and the other end of drain pipe is communicated in the room that is connected with said pumping pipe.

As preferred version; The reaction chamber that wherein said hydrogen or methane generate further includes at least one reflux unit; It has a reflux pump, and reflux pump is connected with a pumping pipe, and the other end of pumping pipe is communicated in a wherein room of said first housing; Reflux pump also is connected with a drain pipe simultaneously, and the other end of drain pipe is communicated in another room between said pumping pipe and said front end.

As preferred version, wherein said drain pipe is connected in the bottom of said room.

As preferred version, the reaction chamber that wherein said hydrogen or methane generate further includes one second housing, and it is sheathed on the outside of one first housing, and and said first housing between possess a spacing and be formed with a keeping warmth space.

As preferred version, the reaction chamber that wherein said hydrogen or methane generate further includes a cycling element, and it has a recycle pump, and recycle pump is connected with a drinking-water pipe and a rising pipe, and the other end of said drinking-water pipe and rising pipe is communicated in said keeping warmth space.

As preferred version, the outside of wherein said first housing also is arranged with a thermal insulation layer.

The reaction chamber that the hydrogen that the utility model provided or methane generate, the user can inject this room by this inlet with the mixing liquid that mixed by matrix, mikrobe and water etc., is provided with this dividing plate because of between said room at this moment; Flow to another room and can hinder this mixing liquid by a room wherein; And make the speed of this mixing liquid through said perforation greater than mobile speed in this room, it is mobile to circle round in each room so this mixing liquid will be influenced by coherence, therefore; Not only can this matrix of disturbance and this mikrobe; Mixing this matrix and this mikrobe equably, and can increase this mixing liquid and rest on the time in this room, and this matrix and this mikrobe can be reacted fully; And then can significantly promote the production capacity of hydrogen or methane, to reach the purpose of promoting preparation hydrogen or methane efficient.

Description of drawings

Fig. 1 is the synoptic diagram of the reaction chamber of a kind of known hydrogen or methane generation;

Fig. 2 is the cross-sectional schematic of the utility model preferred embodiment;

Fig. 3 is the use synoptic diagram of the utility model preferred embodiment;

Fig. 4 is the use synoptic diagram of another preferred embodiment of the utility model.

[main element nomenclature]

Cell body-1; First housing-10; The reaction chamber-100 that hydrogen or methane generate; Front end-11; Rear end-12; Dividing plate-13; Perforation-131; Room-14; Inlet-15; Outlet-16; Bypass outlet-17; Reflux inlet-18;

Dividing plate-2; Reflux unit-20; Reflux pump-21; Pumping pipe-22; Drain pipe-23;

Rising runner-3; Second housing-30; Loop exit-31; Loop head-32;

Decline runner-4; Keeping warmth space-40;

Inlet-5; Cycling element-50; Recycle pump-51; Drinking-water pipe-52; Rising pipe-53;

Outlet-6; Thermal insulation layer-60.

Embodiment

In order further to understand the characteristic and the technology contents of the utility model, see also following detailed description and accompanying drawing, yet it only provides the usefulness of reference with explanation about the utility model, be not to be used to limit the utility model.

See also shown in Figure 2ly, be the sectional view of the utility model preferred embodiment, the reaction chamber 100 that its announcement has a kind of hydrogen or methane to generate, the reaction chamber 100 that said hydrogen or methane generate consists predominantly of:

One first housing 10; It is arranged transversely; And have the rear end 12 that a front end 11 and is oppositely arranged, also vertically stand in first housing 10 simultaneously and be provided with at least one dividing plate 13, and be equipped with most perforation 131 on the dividing plate 13; So that can be formed with at least two rooms 14 in regular turn by front end 11 rearward end 12 directions in first housing 10, and said room 14 can interconnect; In the present embodiment, be provided with two dividing plates 13 in first housing 10, and be formed with three rooms 14; In addition; First housing 10 also is equipped with an inlet 15 in front end 11 positions, and enters the mouth and 15 be connected with the room 14 of

adjacent front end

11, and 12 positions also are equipped with one and export 16 first housing 10 in the rear end; And exporting 16 is connected with the room 14 of adjacent back end 12; Simultaneously all sides of first housing 10 also are equipped with a bypass outlet 17, and bypass outlet 17 is connected with the room 14 of adjacent front end 11, and all sides of first housing 10 also are equipped with a reflux inlet 18 in addition; And reflux inlet 18 is connected with the room 14 of adjacent front end 11, and is positioned at the bottom of said room 14.

At least one reflux unit 20; It has a reflux pump 21; And reflux pump 21 is connected with a pumping pipe 22; The other end of pumping pipe 22 is communicated in a wherein room 14 of first housing 10, and reflux pump 21 also is connected with a drain pipe 23 simultaneously, and the other end of drain pipe 23 is communicated in the room 14 that is connected with pumping pipe 22; In the present embodiment; The reaction chamber 100 that said hydrogen or methane generate has a reflux unit 20; And the pumping pipe 22 of reflux unit 20 is connected in bypass outlet 17; Drain pipe 23 then is connected in reflux inlet 18, so that pumping pipe 22 can be communicated in the room 14 of adjacent front end 11 with drain pipe 23, and makes drain pipe 23 be connected in the bottom of room 14.

One second housing 30; It is sheathed on the outside of one first housing 10; And and 10 of first housings possess a spacing and be formed with a keeping warmth space 40, simultaneously all sides of second housing 30 also are equipped with a loop exit 31 and a loop head 32 that communicates with keeping warmth space 40.

One cycling element 50, it has a recycle pump 51, and recycle pump 51 is connected with a drinking-water pipe 52 and a rising pipe 53, and drinking-water pipe 52 is communicated in keeping warmth space 40 with the other end of rising pipe 53; In the present embodiment, drinking-water pipe 52 is connected in loop exit 31, and rising pipe 53 then is connected in loop head 32, so that the other end of drinking-water pipe 52 and rising pipe 53 can be communicated in keeping warmth space 40.

Please consult shown in Figure 3ly more simultaneously, be the use synoptic diagram of the utility model preferred embodiment, the user can inject first housing 10 by inlet 15 with the mixing liquid that mixed by matrix, mikrobe and water etc.; And letting this mixing liquid by front end 11 rearward end 12 directions, each room 14 is flow through in the perforation 131 of passing in regular turn on the said dividing plate 13, discharges first housing 10 by outlet 16 again; Wherein, Because 14 of said rooms are provided with dividing plate 13, flow to another room 14 and can hinder this mixing liquid by a room 14 wherein, and make the speed of this mixing liquid through said perforation 131 greater than mobile speed in room 14; So this mixing liquid will be influenced by coherence and in each room 14, circle round mobile; Therefore, not only can this matrix of disturbance and this mikrobe, to mix this matrix and this mikrobe equably; And can increase this mixing liquid and rest on the time in the room 14; And this matrix and this mikrobe can be reacted fully, and then can significantly promote the production capacity of hydrogen or methane, to reach the purpose of promoting preparation hydrogen or methane efficient.

What deserves to be mentioned is; Through the reflux pump 21 of reflux unit 20, more can extract this mixing liquid out room 14 by bypass outlet 17, and via the guiding of pumping pipe 22 with drain pipe 23; Again send this mixing liquid back to room 14 by reflux inlet 18; So not only can further prolong this mixing liquid and rest on the time in the room 14, and because backflow gangway 18 is arranged at the bottom of room 14, so more can be as this mixing liquid of disturbance as the spring; Make this matrix more even, thereby can further promote the efficient of preparation hydrogen or methane with mixing of this mikrobe.

What be worth carrying is again, the user can be with a heat insulation liquid, like water etc.; Be injected in the keeping warmth space 40; And the recycle pump 51 through cycling element 50 extracts this heat insulation liquid out keeping warmth spaces 40 by the loop exit 31 of second housing 30, through the guiding of this drinking-water pipe 52 with this rising pipe 53, sends this heat insulation liquid back to keeping warmth space 40 by loop head 32 again again; Flow in keeping warmth space 40 to drive this heat insulation liquid; Therefore, can keep the temperature in the said room 14, this matrix and this mikrobe can be reacted under the temperature of reaction of the best through this heat insulation liquid.

Please consult shown in Figure 4 more simultaneously; Use synoptic diagram for another preferred embodiment of the utility model; Reaction chamber 100 and aforementioned preferred embodiment difference that said hydrogen or methane generate are; The bypass outlet 17 of first housing 10 is connected with the room 14 of adjacent back end 12; Reflux inlet 18 then is connected with the room 14 of adjacent front end 11, so that the other end of the pumping pipe 22 of reflux unit 20 can be communicated in a wherein room 14 of first housing 10, the other end of drain pipe 23 then is communicated in another room 14 of 11 of pumping pipe 22 and front ends; Can supply this mixing liquid is drawn back the room 14 to adjacent front end 11 by the room 14 of adjacent back end 12, rest on the time in the room 14 to increase this mixing liquid; In addition, in the present embodiment, the outside of first housing 10 directly is provided with a thermal insulation layer 60 thoroughly, and for example therefore Baolilong layer etc., can reach the effect identical with aforementioned preferred embodiment.

The above; Be merely the preferred embodiment of the utility model; Be not scope of patent protection,, all should in like manner be contained within the scope of patent protection of the utility model so use spiritual equivalent structure variation of being done of the patent of the utility model or modification etc. such as in order to restriction the utility model.

Claims

1. the reaction chamber that generates of hydrogen or methane; It is characterized in that the reaction chamber that said hydrogen or methane generate includes first housing of an arranged transversely, and first housing has the rear end that a front end and is oppositely arranged; Also vertically stand in first housing simultaneously and be provided with at least one dividing plate; Be equipped with most perforation on the said dividing plate, and extreme direction is formed with at least two rooms in regular turn towards said back by said front end in said first housing, said room is connected; And first housing also is equipped with an inlet at said front position place; And inlet is connected with the room of contiguous said front end, and first housing also is equipped with an outlet at said back-end location place, and outlet is connected with the room of contiguous said rear end.

2. the reaction chamber that a kind of hydrogen as claimed in claim 1 or methane generate; It is characterized in that the reaction chamber that said hydrogen or methane generate further includes at least one reflux unit, it has a reflux pump; And reflux pump is connected with a pumping pipe; The other end of pumping pipe is communicated in a wherein room of said first housing, and reflux pump also is connected with a drain pipe simultaneously, and the other end of drain pipe is communicated in the room that is connected with said pumping pipe.

3. the reaction chamber that a kind of hydrogen as claimed in claim 1 or methane generate; It is characterized in that the reaction chamber that said hydrogen or methane generate further includes at least one reflux unit, it has a reflux pump; And reflux pump is connected with a pumping pipe; The other end of pumping pipe is communicated in a wherein room of said first housing, and reflux pump also is connected with a drain pipe simultaneously, and the other end of drain pipe is communicated in another room between said pumping pipe and said front end.

4. like the reaction chamber of claim 2 or 3 described a kind of hydrogen or methane generation, it is characterized in that said drain pipe is connected in the bottom of said room.

5. the reaction chamber that a kind of hydrogen as claimed in claim 1 or methane generate; It is characterized in that; The reaction chamber that said hydrogen or methane generate further includes one second housing, and it is sheathed on the outside of one first housing, and and said first housing between possess a spacing and be formed with a keeping warmth space.

6. the reaction chamber that a kind of hydrogen as claimed in claim 5 or methane generate; It is characterized in that; The reaction chamber that said hydrogen or methane generate further includes a cycling element; It has a recycle pump, and recycle pump is connected with a drinking-water pipe and a rising pipe, and the other end of said drinking-water pipe and rising pipe is communicated in said keeping warmth space.

7. the reaction chamber that a kind of hydrogen as claimed in claim 1 or methane generate is characterized in that the outside of said first housing also is arranged with a thermal insulation layer.