CN200986178Y - Pressure charging type vapor recovery device - Google Patents
Pressure charging type vapor recovery device Download PDFInfo
- Publication number
- CN200986178Y CN200986178Y CN 200620148097 CN200620148097U CN200986178Y CN 200986178 Y CN200986178 Y CN 200986178Y CN 200620148097 CN200620148097 CN 200620148097 CN 200620148097 U CN200620148097 U CN 200620148097U CN 200986178 Y CN200986178 Y CN 200986178Y
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- steam
- vapor
- pressurizer tank
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Abstract
The utility model relates to a pressure charged vapor recoverer, which comprises: a pressurizer tank, a vapor pump set, a vapor compressor set, a steam separating tank, a gate valve, a control valve, a backflow connection, an electrical control system and so on. The 0.005 Ma vapor with a temperature of over 30 DEG C can be pumped out and is compressed into highly compressed steam by the vapor compressor, and then the highly compressed stem is separated into air and water by the steam separating tank, and finally, the air and water are respectively sent out for utilization. The pressure of the pressurizer tank can be always kept by the gate valve and backflow connection equal to less than that of the waste steam discharged by the steam equipment, at the same time, the normal operation of the steam equipment cannot be affected. The whole process of vapor recovery takes place automatically. The utility model can be used for the waste recovery of all industrial and civil vapor systems.
Description
Technical field
The utility model relates to a kind of Steam Recovery device.
Background technology
At present, domestic steam heating system emits vapour and low temperature vapour to efflux phenomenon to exist everywhere, causes a large amount of thermal waste and to the thermal pollution of atmosphere.The method of the useful cold water spray of exhaust steam, high steam or water jet, cold water pipe heat exchange is recycled, and all is that the form with water reclaims.A production line steam and a condensation water recovery system introduced in " carton enterprise: scrap build reduce cost side " literary composition on July in 2006 Chinese environmental protection on the 7th internet: " condensed water and the exhaust steam that production line produced; after the principle pressurization with the piston type cylinder compression; gas-vapor mix is directly compressed into boiler, make boiler with vapour point and airtight circulatory system of Steam Recovery machine formation." above exhaust steam recovery method respectively has its advantage, all is not suitable for the very big Steam Recovery of quantity of steam.Application for a patent for invention number: 03137150.7 exhaust steam in steam turbine recover, introduced: " mechanical energy that converts to electric energy adds the low temperature waste vapour and is pressed into high-temperature water and vapour, is used for factory steam and civil heating refrigeration." there are not detailed embodiment and a description of drawings.
The utility model content
The technical problems to be solved in the utility model is: a kind of device that the low-pressure low-temperature steam pressurized can be become high steam to recycle is provided, and guarantees not influence the operate as normal that produces low-pressure low-temperature exhaust steam equipment.
For solving the problems of the technologies described above, the utility model booster-type Steam Recovery device, it comprises pressurizer tank, gate valve, control valve, return duct, the unit that draws gas, presses steam turbine group, carbonated drink splitter cylinder.This structural design can directly be compressed into the low pressure exhaust steam high-pressure and high-temperature steam and recycle.
Pressurizer tank of the present utility model has the conical pipe outlet of the air intake and the band guiding device of band anemostat, can make steadily inflow of waste vapour, voltage stabilizing, steadily flow out.Return duct of the present utility model, one terminates on the carbonated drink splitter cylinder, and an end is connected on the pressurizer tank through control valve.The aperture of control valve on the adjusting return duct and adjusting gate valve can be regulated the pressure of pressurizer tank, makes the interior pressure of pressurizer tank all the time less than the steam pressure that produces the discharge of waste vapour equipment, guarantees that the operation of booster-type Steam Recovery device does not influence the work that produces waste vapour equipment.
There is liquid level gauge the steam-water separator side, and isolated a small amount of condensate water is drained recovery automatically according to the height of liquid level.
Booster-type Steam Recovery device is furnished with electric-control system, and the overall process of Steam Recovery is carried out automatically.
Description of drawings
Below in conjunction with accompanying drawing the utility model is described in further details.
Fig. 1 is the view of the utility model booster-type Steam Recovery device embodiment.
Fig. 2 is the cutaway view of the utility model pressurizer tank.
The specific embodiment
Fig. 1 shows the utility model embodiment, and it comprises pressurizer tank (1), gate valve (2), control valve (3), return duct (4), the unit of bleeding (5), presses steam turbine group (6) carbonated drink splitter cylinder (7).On the one termination carbonated drink splitter cylinder (7) of return duct (4), the other end is connected on the pressurizer tank (1) through control valve (3).
Fig. 2 shows the cutaway view of the utility model pressurizer tank.Pressurizer tank (1) has the air intake (8) of band anemostat and the conical pipe venthole of band guiding device (9).
The low-pressure low-temperature exhaust steam that gas utilization unit produces enters pressurizer tank (1) by the air intake (8) of band anemostat, pressure in the pressurizer tank (1) is regulated by the backflow of its unit of bleeding (5), gate valve (2) and return duct (4), makes the interior pressure of pressurizer tank (1) be equal to or less than the pressure of the waste vapour of gas utilization unit discharge all the time.Steam in the pressurizer tank (1) is taken away through band conical pipe venthole (8), gate valve (2) unit (5) of being bled, and is compacted into the steam of high pressure-temperature in pressing steam turbine (6), carbonated drink separation carbonated drink splitter cylinder (7) in, and carbonated drink is seen off reuse respectively.
Booster-type Steam Recovery device is furnished with pressure sensor, thermometer, liquid level gauge, electric cabinet, and the overall process of Steam Recovery is carried out automatically.
The utility model is a kind of equipment that high steam is recycled that is pressed into that directly exhaust steam added, heat-energy losses is few, the organic efficiency height, the waste vapour that not only can be used for general industry and civilian vapour system reclaims, and also can be used for the recovery of the low-pressure low-temperature steam that equipment such as steam turbine produces.
Claims (2)
1. booster-type Steam Recovery device, it comprises pressurizer tank, gate valve, control valve, return duct, the unit that draws gas, presses steam turbine group, carbonated drink splitter cylinder, it is characterized in that: described pressurizer tank (1) has the air intake (8) of band anemostat and the taper venthole of band guiding device (9).
2. booster-type Steam Recovery device according to claim 1 is characterized in that: described return duct (4), and one terminates on the carbonated drink splitter cylinder (7), and an end is connected on the pressurizer tank (1) through control valve (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620148097 CN200986178Y (en) | 2006-10-25 | 2006-10-25 | Pressure charging type vapor recovery device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620148097 CN200986178Y (en) | 2006-10-25 | 2006-10-25 | Pressure charging type vapor recovery device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN200986178Y true CN200986178Y (en) | 2007-12-05 |
Family
ID=38915635
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620148097 Expired - Fee Related CN200986178Y (en) | 2006-10-25 | 2006-10-25 | Pressure charging type vapor recovery device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN200986178Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103629085A (en) * | 2013-12-03 | 2014-03-12 | 山东威普斯橡胶股份有限公司 | Waste steam pressurizing and recovering equipment for thermal power plant |
| WO2015120570A1 (en) * | 2014-02-11 | 2015-08-20 | 刘凯 | Solar-powered autoclave device |
| CN109210378A (en) * | 2018-09-26 | 2019-01-15 | 上海慧得节能科技有限公司 | A kind of system for eliminating steam surplus using pressure-raising |
-
2006
- 2006-10-25 CN CN 200620148097 patent/CN200986178Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103629085A (en) * | 2013-12-03 | 2014-03-12 | 山东威普斯橡胶股份有限公司 | Waste steam pressurizing and recovering equipment for thermal power plant |
| WO2015120570A1 (en) * | 2014-02-11 | 2015-08-20 | 刘凯 | Solar-powered autoclave device |
| CN109210378A (en) * | 2018-09-26 | 2019-01-15 | 上海慧得节能科技有限公司 | A kind of system for eliminating steam surplus using pressure-raising |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |