CN202630006U - Closed ultrahigh temperature condensed water recycling device - Google Patents
Closed ultrahigh temperature condensed water recycling device Download PDFInfo
- Publication number
- CN202630006U CN202630006U CN 201220282329 CN201220282329U CN202630006U CN 202630006 U CN202630006 U CN 202630006U CN 201220282329 CN201220282329 CN 201220282329 CN 201220282329 U CN201220282329 U CN 201220282329U CN 202630006 U CN202630006 U CN 202630006U
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- temperature
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- condensed water
- distillation plant
- flash distillation
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Abstract
The utility model discloses a closed ultrahigh temperature condensed water recycling device. The closed ultrahigh temperature condensed water recycling device comprises a high-pressure high-temperature flashing device, a high-pressure jet ejecting device, a high temperature condensed water pressurizing and conveying device and a control cabinet, wherein the high-pressure high-temperature flashing device is connected with the high-pressure jet ejecting device and the high temperature condensed water pressurizing and conveying device respectively; and the control cabinet is connected with the high-pressure high-temperature flashing device, the high-pressure jet ejecting device and the high temperature condensed water pressurizing and conveying device respectively. The closed ultrahigh temperature condensed water recycling device utilizes heat energy and mechanical energy, effectively reduces pollution, is reasonable and compact in structure and convenient to use, and saves the cost.
Description
Technical field
The utility model relates to the apparatus for recovering technical field, particularly relates to a kind of superhigh temperature condensate enclosed retracting device.
Background technology
Existing condensed-water recovering device; Basically can only rest on the recovery basis below 120 ℃,, not have good processing mode basically being higher than 150 ℃ perhaps 180 ℃ of this temperature; Not that sky is discharged; Add the heat exchange of cold water refrigeration exactly, heat energy and the mechanical energy that can not finely utilize secondary vapour to be had cause potential waste.
The utility model content
The main purpose of the utility model is to overcome the deficiency of prior art, and a kind of superhigh temperature condensate enclosed retracting device is provided.
To achieve these goals; The technical solution of the utility model provides a kind of superhigh temperature condensate enclosed retracting device; Comprise high pressure-temperature flash distillation plant, high-pressure injection induction apparatus and condensed water in high temperature supercharging transport, said high pressure-temperature flash distillation plant links to each other with condensed water in high temperature supercharging transport with said high-pressure injection induction apparatus respectively;
Said high pressure-temperature flash distillation plant comprises condensed water in high temperature water inlet, condensed water in high temperature delivery port, secondary flash steam venthole, first safety valve and first liquid level gauge;
Said condensed water in high temperature supercharging transport comprises condensed water in high temperature water tank, second liquid level gauge, second safety valve, a plurality of water inlet and delivery port, and said condensed water in high temperature water tank links to each other with delivery port with said second liquid level gauge, second safety valve, a plurality of water inlet respectively;
Said high-pressure injection induction apparatus comprises the high steam air intake; Injection vapour air intake; Middle pressure steam venthole and pressure flow by-pass valve control; Said high-pressure injection induction apparatus respectively with said high steam air intake, by injection vapour air intake, the middle pressure steam venthole links to each other with the pressure flow by-pass valve control.
Further; Said condensed water in high temperature water inlet is positioned at said high pressure-temperature flash distillation plant centre position; Said condensed water in high temperature delivery port is positioned at the bottom of said high pressure-temperature flash distillation plant; Said secondary flash steam venthole is positioned at said high pressure-temperature flash distillation plant top, and said first safety valve is positioned at the top of said secondary flash steam venthole, and it is inner that said first liquid level gauge is positioned at said high pressure-temperature flash distillation plant.
Further, said retracting device adopts the skid form.
Further, also be provided with check-valves on the said secondary flash steam venthole.
Further, also comprise pressure sensor in the said high pressure-temperature flash distillation plant.
Further, said high-pressure injection induction apparatus also comprises mixing tube, diffuser pipe and with the steam pipe network.
Further, said retracting device also comprises switch board, and said switch board links to each other with said high pressure-temperature flash distillation plant, high-pressure injection induction apparatus and condensed water in high temperature supercharging transport respectively.
Adopt technique scheme, the beneficial effect of the utility model is:
Utilize heat energy and mechanical energy, effectively reduce pollution, rational in infrastructure, compact, easy to use, saving cost.
Description of drawings
Fig. 1 is the structural representation of a kind of superhigh temperature condensate enclosed retracting device of the utility model.
The specific embodiment
Below in conjunction with accompanying drawing, the specific embodiment of the utility model is described in further detail.Following examples are used to explain the utility model, but are not used for limiting the scope of the utility model.
The structural representation of the superhigh temperature condensate enclosed retracting device of the utility model is as shown in Figure 1; Comprise high pressure-temperature flash distillation plant 2, high-pressure injection induction apparatus 16, condensed water in high temperature supercharging transport 1 and switch board 18; Said high pressure-temperature flash distillation plant 2 links to each other with condensed water in high temperature supercharging transport 1 with said high-pressure injection induction apparatus respectively, and said switch board 18 links to each other with condensed water in high temperature supercharging transport 1 with said high pressure-temperature flash distillation plant 2, high-pressure injection induction apparatus 16 respectively;
Said high pressure-temperature flash distillation plant 2 comprises condensed water in high temperature water inlet 15, condensed water in high temperature delivery port 10, secondary flash steam venthole 12, first safety valve 11 and first liquid level gauge 9;
Said condensed water in high temperature supercharging transport 1 comprises condensed water in high temperature water tank, second liquid level gauge 3, second safety valve 4, a plurality of water inlet 5 and delivery port, and said condensed water in high temperature water tank links to each other with delivery port with said second liquid level gauge 3, second safety valve 4, a plurality of water inlet 5 respectively;
Said high-pressure injection induction apparatus 16 comprises the high steam air intake; Injection vapour air intake; Middle pressure steam venthole and pressure flow by-pass valve control 14; Said condensed water in high temperature water inlet 15 is positioned at said high pressure-temperature flash distillation plant 2 centre positions, and said condensed water in high temperature delivery port 10 is positioned at the bottom of said high pressure-temperature flash distillation plant 2, and said secondary flash steam venthole 12 is positioned at said high pressure-temperature flash distillation plant 2 tops; Said first safety valve 11 is positioned at the top of said secondary flash steam venthole 12, and said first liquid level gauge 9 is positioned at said high pressure-temperature flash distillation plant 2 inside.
Said retracting device adopts the skid form.
Also be provided with check-valves 13 on the said secondary flash steam venthole 12.
Also comprise pressure sensor in the said high pressure-temperature flash distillation plant 2.
Said high-pressure injection induction apparatus 16 also comprises mixing tube, diffuser pipe and with the steam pipe network.
The superhigh temperature condensate is introduced into condensed water in high temperature water inlet 15; After 2 separation of high pressure-temperature flash distillation plant; Flash distillation secondary vapour gets into high-pressure injection induction apparatus 16 after high pressure-temperature flash distillation plant 2 internal pressures arrive setting pressure from secondary flash steam venthole 12; By pressure sensor pressure signal is sent to switch board 18, sends operating instruction by switch board 18 to first safety valve 11, secondary vapour gets into the injection air intake in the high-pressure injection induction apparatus 16 under pressure; Regulating high steam by pressure flow by-pass valve control 14 sprays secondary vapour injection to high pressure in the mixing tube of induction apparatus 16; In mixing tube, mix the back and get into diffuser pipe, supply with the steam pipe network by setting pressure and replenish vapour, high-pressure injection induction apparatus 16 1 ends are equipped with pressure detecting table 17; Regulate pressure flow by-pass valve control 14, realize that middle pressure steam is stable.
The superhigh temperature condensate is after 2 flash distillations of high pressure-temperature flash distillation plant; With saturated high-temperature condensation water under the pressure from secondary flash steam venthole 12; Get into condensed water in high temperature supercharging transport 1 through motor-driven valve 7, can move automatically, realize that the liquid level in the high pressure-temperature flash distillation plant 2 is basicly stable by first liquid level gauge, 9 situation in the high pressure-temperature flash distillation plant 2; Motor-driven valve 7 has by-passing valve 8, uses as trouble hunting.
Behind motor-driven valve 7; The saturated condensate of high temperature leans on self pressure to get into the water inlet 5 of condensed water in high temperature supercharging transport 1; Condensate is collected in the condensed water in high temperature water tank; After certain liquid level, by second liquid level gauge 3 signal is transferred to switch board 18, control two and go out liquid level substantially constant in the water pump 19 realization condensed water in high temperature water tanks, pressurized condensed water in high temperature is delivered to water occasions such as oxygen-eliminating device.
The utility model utilize heat energy and mechanical energy, effectively reduce pollution, rational in infrastructure, compact, easy to use, practice thrift cost.
Said only is the preferred implementation of the utility model; Should be pointed out that for those skilled in the art, under the prerequisite that does not break away from know-why of the present invention; Can also make some improvement and retouching, these improvement and retouching also should be regarded as protection scope of the present invention.
Claims (7)
1. superhigh temperature condensate enclosed retracting device; It is characterized in that; Comprise high pressure-temperature flash distillation plant, high-pressure injection induction apparatus and condensed water in high temperature supercharging transport, said high pressure-temperature flash distillation plant links to each other with condensed water in high temperature supercharging transport with said high-pressure injection induction apparatus respectively;
Said high pressure-temperature flash distillation plant comprises condensed water in high temperature water inlet, condensed water in high temperature delivery port, secondary flash steam venthole, first safety valve and first liquid level gauge;
Said condensed water in high temperature supercharging transport comprises condensed water in high temperature water tank, second liquid level gauge, second safety valve, a plurality of water inlet and delivery port, and said condensed water in high temperature water tank links to each other with delivery port with said second liquid level gauge, second safety valve, a plurality of water inlet respectively;
Said high-pressure injection induction apparatus comprises the high steam air intake; Injection vapour air intake; Middle pressure steam venthole and pressure flow by-pass valve control; Said high-pressure injection induction apparatus respectively with said high steam air intake, by injection vapour air intake, the middle pressure steam venthole links to each other with the pressure flow by-pass valve control.
2. superhigh temperature condensate enclosed retracting device according to claim 1; It is characterized in that; Said condensed water in high temperature water inlet is positioned at said high pressure-temperature flash distillation plant centre position, and said condensed water in high temperature delivery port is positioned at the bottom of said high pressure-temperature flash distillation plant, and said secondary flash steam venthole is positioned at said high pressure-temperature flash distillation plant top; Said first safety valve is positioned at the top of said secondary flash steam venthole, and it is inner that said first liquid level gauge is positioned at said high pressure-temperature flash distillation plant.
3. superhigh temperature condensate enclosed retracting device according to claim 1 is characterized in that, said retracting device adopts the skid form.
4. superhigh temperature condensate enclosed retracting device according to claim 2 is characterized in that, also is provided with check-valves on the said secondary flash steam venthole.
5. superhigh temperature condensate enclosed retracting device according to claim 1 is characterized in that, also comprises pressure sensor in the said high pressure-temperature flash distillation plant.
6. superhigh temperature condensate enclosed retracting device according to claim 1 is characterized in that, said high-pressure injection induction apparatus also comprises mixing tube, diffuser pipe and with the steam pipe network.
7. according to each described superhigh temperature condensate enclosed retracting device of claim 1 to 6; It is characterized in that; Said retracting device also comprises switch board, and said switch board links to each other with said high pressure-temperature flash distillation plant, high-pressure injection induction apparatus and condensed water in high temperature supercharging transport respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220282329 CN202630006U (en) | 2012-06-15 | 2012-06-15 | Closed ultrahigh temperature condensed water recycling device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220282329 CN202630006U (en) | 2012-06-15 | 2012-06-15 | Closed ultrahigh temperature condensed water recycling device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202630006U true CN202630006U (en) | 2012-12-26 |
Family
ID=47383201
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220282329 Expired - Lifetime CN202630006U (en) | 2012-06-15 | 2012-06-15 | Closed ultrahigh temperature condensed water recycling device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202630006U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103123107A (en) * | 2013-03-06 | 2013-05-29 | 宁波金海德旗化工有限公司 | Device for recovering waste heat and supplying steam through multistage dilatation flashing |
| CN103438428A (en) * | 2013-08-27 | 2013-12-11 | 重庆瑞宝环保工程有限公司 | Closed steam condensate water high-temperature recovery system |
| CN105546514A (en) * | 2016-01-26 | 2016-05-04 | 山东舜业热能科技有限公司 | Closed type condensation water recycling device |
| CN106352322A (en) * | 2016-08-26 | 2017-01-25 | 湖南柯林瀚特环保科技有限公司 | Vapor-liquid micro-negative pressure condensed water recycling system |
-
2012
- 2012-06-15 CN CN 201220282329 patent/CN202630006U/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103123107A (en) * | 2013-03-06 | 2013-05-29 | 宁波金海德旗化工有限公司 | Device for recovering waste heat and supplying steam through multistage dilatation flashing |
| CN103438428A (en) * | 2013-08-27 | 2013-12-11 | 重庆瑞宝环保工程有限公司 | Closed steam condensate water high-temperature recovery system |
| CN105546514A (en) * | 2016-01-26 | 2016-05-04 | 山东舜业热能科技有限公司 | Closed type condensation water recycling device |
| CN106352322A (en) * | 2016-08-26 | 2017-01-25 | 湖南柯林瀚特环保科技有限公司 | Vapor-liquid micro-negative pressure condensed water recycling system |
| CN106352322B (en) * | 2016-08-26 | 2017-08-29 | 湖南柯林瀚特环保科技有限公司 | A kind of vapour-liquid shunts tiny structure steam condensate recovery system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20121226 |