CN207871829U - A kind of garbage loading embeading Marsh gas compression postcooling and steam-water separation system - Google Patents
A kind of garbage loading embeading Marsh gas compression postcooling and steam-water separation system Download PDFInfo
- Publication number
- CN207871829U CN207871829U CN201820090524.8U CN201820090524U CN207871829U CN 207871829 U CN207871829 U CN 207871829U CN 201820090524 U CN201820090524 U CN 201820090524U CN 207871829 U CN207871829 U CN 207871829U
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- Prior art keywords
- steam
- sieve
- spiral
- postcooling
- plate tower
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Abstract
The utility model discloses a kind of garbage loading embeading Marsh gas compression postcooling and steam-water separation systems, including spiral separation cylinder and support baseboard, sieve-plate tower is installed above the support baseboard, the side of the sieve-plate tower is equipped with separation motor, the other side of the sieve-plate tower is equipped with kinetic pump, the top of the spiral separation cylinder is equipped with vibrator, power-on box is installed below the feed inlet, control panel is installed at the front surface center of the power-on box, the inside of the spiral separation cylinder is equipped with solid-liquid dry and wet adjustable device, spiral propeller is installed below the solid-liquid dry and wet adjustable device.The utility model is provided with return pipe connecting valve, cycle separating for several times can be carried out to steam, and then can improve processing effect, improves disintegrate-quality；It is provided with solid-liquid dry and wet adjustable device, the actual power of body can be automatically adjusted, and then reaches reduction operating power consumption, the effect of effect of optimization.
Description
Technical field
The utility model is related to piece-rate system technical field, specifically a kind of garbage loading embeading Marsh gas compression postcooling and carbonated drink
Piece-rate system.
Background technology
Gravity Separation is carried out using carbonated drink density contrast；Using flow direction is changed, carries out inertial separation and revolved using steam flow
Centrifugal force when transhipment is dynamic carries out carbonated drink centrifugation；Formation is flowed down using making water adhesion form moisture film on the metal surface
The device of the steam-water separations such as adsorbing separation is known as water separator.
For the separation equipment of liquid mixture, in addition to the method that distillation can be used, the method that extraction also can be used exists
A liquid substantially not miscible with it is added in liquid mixture (material liquid) as solvent, causes the second phase, utilizes original
Different solubility of each component in two liquid phases in feed liquid and so that raw material liquid mixture is detached.Liquid-liquid extraction, it is also known as molten
Agent extracts, and referred to as extracts or extracts.The solvent of selection is known as extractant, is indicated with S；The component of S is soluble in material liquid, referred to as
Solute is indicated with A；The component for being insoluble in S is known as former solvent (or diluent), is indicated with B.If in extraction process, extractant
Component related in material liquid does not chemically react, then referred to as physical extraction, on the contrary then be referred to as chemical extraction.
There are many shortcomings in traditional separator, energy loss is big in actual use, and separating effect is bad etc.
Problem, therefore a kind of garbage loading embeading Marsh gas compression postcooling and steam-water separation system are needed for solving the above problems.
Utility model content
The purpose of this utility model is to provide a kind of garbage loading embeading Marsh gas compression postcooling and steam-water separation systems, with solution
Certainly the problems of the prior art.
To achieve the above object, the utility model provides the following technical solutions：A kind of garbage loading embeading Marsh gas compression postcooling
With steam-water separation system, including spiral separation cylinder and support baseboard, sieve-plate tower, the sieve are installed above the support baseboard
The side of plate tower is equipped with separation motor, and the other side of the sieve-plate tower is equipped with kinetic pump, and is installed on the surface of sieve-plate tower
There are clips, the spiral separation cylinder to be installed in the top of support baseboard, the top of the spiral separation cylinder is equipped with
Vibrator, and the front surface of spiral separation cylinder is provided with discharge port, and feed inlet, the charging are provided with below the discharge port
The lower section of mouth is equipped with power-on box, control panel is equipped at the front surface center of the power-on box, the control panel is close
The side of sieve-plate tower is equipped with return pipe connecting valve, and the inside of the spiral separation cylinder is equipped with solid-liquid dry and wet adjustable device, institute
It states and spiral propeller is installed below solid-liquid dry and wet adjustable device, live spindle is installed at the center of the spiral propeller.
It is attached by clips between the spiral separation cylinder and sieve-plate tower.
Screw propulsion leaf is provided on the surface of the live spindle.
It is connected by nonproliferation separate tube between the return pipe connecting valve and vibrator.
The bottom end of the support baseboard is equipped with supporting foot, and there are four supporting foot is arranged altogether.
Compared with prior art, the utility model has the beneficial effects that：The utility model is scientific and reasonable for structure, safe to use
Convenient, in the side wall of shell and bottom to insulating layer, a part for nonproliferation separate tube is placed in shell, the top of shell and exciting
Be fixedly connected at the top of device, the part of nonproliferation separate tube also be fixedly connected at the top of vibrator.Using double-layer structure to vapour with
Water is detached, and thermal energy is taken full advantage of, and is not required to install drain water piping in the external of vibrator, is reduced heat-energy losses, improve
The thermal efficiency and steam quality make the water content in steam be far below 3% index of national regulation；It is provided with return pipe connection
Valve can carry out steam cycle separating for several times, and then can improve processing effect, improve disintegrate-quality；It is provided with solid-liquid
Dry and wet adjustable device, can automatically adjust the actual power of body, and then reach reduction operating power consumption, the effect of effect of optimization.
Description of the drawings
Fig. 1 is the structural schematic diagram of the utility model.
Fig. 2 is the sectional view of the utility model.
In figure：The nonproliferation separate tube of 1- vibrators, 2-, 3- spiral separations cylinder, 4- discharge ports, 5- feed inlets, 6- power-on box, 7- controls
Panel processed, 8- separation motor, 9- support baseboards, 10- clips, 11- sieve-plate towers, 12- return pipes connecting valve, 13- kinetic pumps,
14- solid-liquid dry and wets adjustable device, 15- spiral propellers, 16- live spindles.
Specific implementation mode
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
The every other embodiment obtained, shall fall within the protection scope of the present invention.
Please refer to Fig.1~2, in the utility model embodiment, a kind of garbage loading embeading Marsh gas compression postcooling and steam-water separation
The top of system, including spiral separation cylinder 3 and support baseboard 9, support baseboard 9 is equipped with sieve-plate tower 11, the side of sieve-plate tower 11
Separation motor 8 is installed, the other side of sieve-plate tower 11 is equipped with kinetic pump 13, and is equipped with clips on the surface of sieve-plate tower 11
10, spiral separation cylinder 3 is installed in the top of support baseboard 9, and the top of spiral separation cylinder 3 is equipped with vibrator 1, and spiral shell
The front surface of rotation cylinder 3 is provided with discharge port 4, and the lower section of discharge port 4 is provided with feed inlet 5, and the lower section of feed inlet 5 is equipped with
Power-on box 6, control panel 7 is equipped at the front surface center of power-on box 6, and control panel 7 is installed close to the side of sieve-plate tower 11
There are return pipe connecting valve 12, the inside of spiral separation cylinder 3 that solid-liquid dry and wet adjustable device 14 is installed, solid-liquid dry and wet adjustable device 14
Lower section is equipped with spiral propeller 15, and live spindle 16 is equipped at the center of spiral propeller 15.Spiral separation cylinder 3 and sieve plate
It is attached by clips 10 between tower 11.Screw propulsion leaf is provided on the surface of live spindle 16.Return pipe connection valve
It is connected by nonproliferation separate tube 2 between door 12 and vibrator 1.The bottom end of support baseboard 9 is equipped with supporting foot, and supporting foot is arranged altogether
There are four.
The operation principle of the utility model is；It is whether normal that each parts are detected when the use first, and then ensure machine
Body can normally work safely, and the top of nonproliferation separate tube 2, vibrator 1 and spiral separation cylinder 3, spiral separation cylinder 3 offers steaming
Vapour entrance, internal setting steam-filtering tube, the upper end of steam-filtering tube communicates with nonproliferation separate tube 2, lower end connection vibrator 1, steam-filtering tube and sharp
The device 11 that shakes collectively forms steam filtration unit, and cavity is formed between the filter element outer wall and the inner wall of spiral separation cylinder.Work as steaming
When vapour is along the helicla flute flowing of spiral separation cylinder 3, level-one steam-water separation is first carried out to it by spiral separation cylinder 3；Steam is through too drastic
Shake device 1 when, then steam-water separation is carried out to it；The water effective in steam can be separated after separation, avoiding steam will
Bacterial endotoxin in moisture and moisture is taken away, and the quality of steam is improved, and then also improves the quality of production of distilled water.
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 practicality is new in other specific forms
Type.Therefore, in all respects, the present embodiments are to be considered as illustrative and not restrictive, this practicality is new
The range of type is indicated by the appended claims rather than the foregoing description, it is intended that containing in the equivalent requirements of the claims will be fallen
All changes in justice and range are embraced therein.Any reference numeral in claim should not be considered as limitation
Involved claim.
Claims (5)
1. a kind of garbage loading embeading Marsh gas compression postcooling and steam-water separation system, including spiral separation cylinder (3) and support baseboard
(9), sieve-plate tower (11) is installed, the side of the sieve-plate tower (11) is equipped with separation motor above the support baseboard (9)
(8), the other side of the sieve-plate tower (11) is equipped with kinetic pump (13), and is equipped with clips on the surface of sieve-plate tower (11)
(10), the spiral separation cylinder (3) is installed in the top of support baseboard (9), and the top of the spiral separation cylinder (3) is pacified
Front surface equipped with vibrator (1), and spiral separation cylinder (3) is provided with discharge port (4), the lower section setting of the discharge port (4)
There is feed inlet (5), power-on box (6) is installed below the feed inlet (5), is pacified at the front surface center of the power-on box (6)
Equipped with control panel (7), the control panel (7) is equipped with return pipe connecting valve (12) close to the side of sieve-plate tower (11),
The inside of the spiral separation cylinder (3) is equipped with solid-liquid dry and wet adjustable device (14), the lower section of the solid-liquid dry and wet adjustable device (14)
Spiral propeller (15) is installed, live spindle (16) is installed at the center of the spiral propeller (15).
2. a kind of garbage loading embeading Marsh gas compression postcooling according to claim 1 and steam-water separation system, it is characterised in that：
It is attached by clips (10) between the spiral separation cylinder (3) and sieve-plate tower (11).
3. a kind of garbage loading embeading Marsh gas compression postcooling according to claim 1 and steam-water separation system, it is characterised in that：
It is provided with screw propulsion leaf on the surface of the live spindle (16).
4. a kind of garbage loading embeading Marsh gas compression postcooling according to claim 1 and steam-water separation system, it is characterised in that：
It is connect by nonproliferation separate tube (2) between the return pipe connecting valve (12) and vibrator (1).
5. a kind of garbage loading embeading Marsh gas compression postcooling according to claim 1 and steam-water separation system, it is characterised in that：
The bottom end of the support baseboard (9) is equipped with supporting foot, and there are four supporting foot is arranged altogether.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820090524.8U CN207871829U (en) | 2018-01-19 | 2018-01-19 | A kind of garbage loading embeading Marsh gas compression postcooling and steam-water separation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820090524.8U CN207871829U (en) | 2018-01-19 | 2018-01-19 | A kind of garbage loading embeading Marsh gas compression postcooling and steam-water separation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207871829U true CN207871829U (en) | 2018-09-18 |
Family
ID=63508003
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820090524.8U Expired - Fee Related CN207871829U (en) | 2018-01-19 | 2018-01-19 | A kind of garbage loading embeading Marsh gas compression postcooling and steam-water separation system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207871829U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115007592A (en) * | 2022-06-20 | 2022-09-06 | 重庆三鑫环保标志有限公司 | Be applied to domestic waste landfill gas collection device |
-
2018
- 2018-01-19 CN CN201820090524.8U patent/CN207871829U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115007592A (en) * | 2022-06-20 | 2022-09-06 | 重庆三鑫环保标志有限公司 | Be applied to domestic waste landfill gas collection device |
| CN115007592B (en) * | 2022-06-20 | 2023-12-15 | 重庆三鑫环保标志有限公司 | Be applied to domestic waste landfill gas collection device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180918 Termination date: 20220119 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |