CN203907225U - Medium pressure high temperature steam control system - Google Patents
Medium pressure high temperature steam control system Download PDFInfo
- Publication number
- CN203907225U CN203907225U CN201420180576.6U CN201420180576U CN203907225U CN 203907225 U CN203907225 U CN 203907225U CN 201420180576 U CN201420180576 U CN 201420180576U CN 203907225 U CN203907225 U CN 203907225U
- Authority
- CN
- China
- Prior art keywords
- outlet
- valve
- flange
- high temperature
- discharge
- Prior art date
- 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
Links
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model relates to a medium pressure high temperature steam control system, comprising a medium pressure high temperature pipeline network; a first manual valve, a filter net, a second manual valve and a metering instrument are arranged in the medium pressure high temperature pipeline network in sequence; a first safety valve and a temperature gauge are arranged at two sides of the metering instrument respectively; a first pressure gauge is arranged at one side of the first safety valve; automatic valves are arranged below the metering instrument; a plurality of heat exchange assemblies are arranged below the automatic valves; a reducing valve and an automatic intelligent valve are arranged below the heat exchange assemblies in sequence; a third pressure gauge and a drain valve are arranged at two sides of the automatic intelligent valve respectively; a second safety valve is arranged at one side of the third pressure gauge; a low temperature area is connected with one side of the second safety valve; a flash evaporator and a common steam pipeline network are connected with one side of the drain valve. The medium pressure high temperature steam control system meets the medium pressure high temperature need in industrial production, generated waste water is applied into other equipment, waste gas is exhausted to the low temperature area, comprehensive resource utilization is realized, and the medium pressure high temperature steam control system is suitable for the application in fields such as a tanning stenter and a thermal needle spinning setting machine.
Description
Technical field
The utility model relates to a kind of control system of steam, specifically relates to super pressure-high temperature steam control system in one, is applied to weaving, printing and dyeing, rubber, process hides, timber processing, oil and foodstuffs processing, the fields such as application baking vanish.
Background technique
Current, to bring direct consequence to us be the more and more serious of haze weather in the develop rapidly of industry, and therefore the burning of the arcola taking coal as raw material is firmly resisted in most areas, eliminates the source of haze weather with this.Therefore, the Some Enterprises rock gas that takes fire, but Gas Prices costliness, cost of production improves greatly, cannot on market, popularize.Steam is because it is cheap and can environment not had a negative impact and is widely used in industrial every field, as weaving, printing and dyeing, rubber, process hides, timber processing, oil and foodstuffs processing, application baking vanish etc. all needs to use the control system of steam to reach the comprehensive utilization of waste heat, and steam is middle super pressure-high temperature, can meet industrial needs.Therefore, those skilled in the art are badly in need of researching and developing a kind of steam control system that can bear middle pressure and high temperature.The utility model produces thus.
Model utility content
For the above-mentioned technical problem of prior art, the purpose of this utility model is to provide super pressure-high temperature steam control system in one, and its heating source using steam as heat exchanger has been realized effective utilization of step waste heat, energy-conserving and environment-protective, and with low cost.
For achieving the above object, the utility model is achieved through the following technical solutions:
Super pressure-high temperature steam control system in one, comprise middle super pressure-high temperature pipe network, described middle super pressure-high temperature pipe network is provided with the first manually operated valve successively, filter screen, the second manually operated valve and gauge, the both sides of described gauge are separately installed with the first safety valve and thermometer, one side of described the first safety valve is provided with the first pressure gauge, the below of described gauge is provided with self-acting valve, the below of described self-acting valve is provided with some heat-exchanging components, the below of described heat-exchanging component is provided with reduction valve and automated intelligent valve successively, the both sides of described automated intelligent valve are separately installed with the 3rd pressure gauge and drain valve, described a 3rd manometric side is provided with the second safety valve, one side of described the second safety valve is connected with low temperature area, one side of described drain valve is connected with flash vessel and common steam pipe network, described heat-exchanging component one side and automated intelligent valve below are all provided with blowdown valve, described heat-exchanging component comprises the 3rd manually operated valve, smart valve, the second pressure gauge, middle super pressure-high temperature steam heating heat exchanger and the single-phase valve that are communicated with successively from top to bottom, and described single-phase valve is communicated with reduction valve.
Described middle super pressure-high temperature steam heating heat exchanger comprises some heat conductive tube connection heat exchange sheets, described heat conductive tube connection heat exchange sheet is metal seamless heat conductive tube connection heat exchange sheet, the outside of heat conductive tube connection heat exchange sheet is coated with radiating fin, and the two ends of heat conductive tube connection heat exchange sheet are all provided with heat conductive tube joining plate, described heat conductive tube joining plate outside is provided with end socket, described heat exchanger is also provided with suction flange, outlet(discharge) flange and dewatering outlet, and described suction flange, outlet(discharge) flange and dewatering outlet are installed on end socket.
Described some heat conductive tube connection heat exchange sheets are that tandem is installed, described suction flange and outlet(discharge) flange are arranged on respectively on two end sockets, described dewatering outlet and outlet(discharge) flange are arranged on same end socket, and dewatering outlet is positioned at outlet(discharge) flange top, and suction flange is relative with dewatering outlet.
Described some heat conductive tubes connection heat exchange sheets are parallel installation, and described suction flange, outlet(discharge) flange and dewatering outlet are arranged on same end socket, and suction flange is positioned at the top of outlet(discharge) flange, and dewatering outlet is arranged on the bottom of end socket.
Described heat exchanger is first horizontal, described some heat conductive tube connection heat exchange sheets are horizontal and arrange left and right, described suction flange, outlet(discharge) flange and dewatering outlet are arranged on same end socket, and suction flange is positioned at the top of outlet(discharge) flange, and dewatering outlet is arranged on the bottom of end socket.
Described heat exchanger is second horizontal, described some heat conductive tube connection heat exchange sheets are longitudinal and arrange left and right, described suction flange and outlet(discharge) flange are arranged on same end socket, and described dewatering outlet is arranged on different end sockets from outlet(discharge) flange, and outlet(discharge) flange is relative with dewatering outlet.
Described heat exchanger is vertical, described some heat conductive tube connection heat exchange sheets are laterally and are arranged above and below, described suction flange and outlet(discharge) flange are arranged on same end socket, suction flange is positioned at outlet(discharge) flange top, described dewatering outlet is arranged on different end sockets from outlet(discharge) flange, and outlet(discharge) flange is relative with dewatering outlet, described heat conductive tube connection heat exchange sheet outside is provided with support, and described support two ends are all connected with heat conductive tube joining plate.
Described radiating fin is circular, square, oval, semicircle or oval nest plate shape.
Described radiating fin is oval.
Described self-acting valve is arranged side by side 2.
The beneficial effects of the utility model are as follows:
1, middle super pressure-high temperature steam control system of the present utility model, super pressure-high temperature pipe network during system before heat-exchanging component adopts, super pressure-high temperature steam heating heat exchanger during heat exchanger adopts, the demand of super pressure-high temperature in having met in industrial production, the waste water producing discharges by drain valve, can be applied in miscellaneous equipment, and the waste gas of generation is emitted on low temperature area by the second safety valve, realize the comprehensive utilization of the energy, be highly suitable for process hides tenter machine, hot pin and spin the field application such as boarding machine.
2, the middle super pressure-high temperature steam heating heat exchanger in the utility model, can bear 30 kilograms of left and right, and pressure maximum is 36 kilograms, and its maximum temperature is 320 DEG C, can meet the needs of the middle super pressure-high temperature of needs in industrial production.Adopt steam heating; can adopt industrial exhaust heat steam as heat exchange source; realize step UTILIZATION OF VESIDUAL HEAT IN; very large contribution is made in the utilization that is not only new energy, and has effectively avoided the haze in boiler burning, has eliminated the source of haze; consistent with the theme of environmental protection; and low price, cost is low, simple to operate.Heat conductive tube connection heat exchange sheet outside is coated with the radiating fin of circle, square, oval, semicircle or oval nest plate shape, and radiating effect is very good.
3, the middle super pressure-high temperature steam heating heat exchanger in the utility model can become tandem, parallel, first horizontal, second horizontal or vertical according to the different Demand Design of commercial Application, meets the arrangement of different industrial production systems.
4, in the utility model, be provided with reduction valve, the pressure in reducing according to actual needs in super pressure-high temperature steam heating heat exchanger, protects follow-up equipment.
5, whether the automated intelligent valve arranging in the utility model can determine closure or openness according to temperature, flow, and not only loss is little, more energy-conservation, has also increased the working life of middle super pressure-high temperature steam heating heat exchanger.
Brief description of the drawings
Fig. 1 is schematic diagram of the present utility model;
Fig. 2 is the external structure schematic diagram of the middle super pressure-high temperature steam heating heat exchanger in the utility model;
Fig. 3 is middle super pressure-high temperature steam heating heat exchanger internal structure schematic diagram of the utility model embodiment 1;
Fig. 4 is middle super pressure-high temperature steam heating heat exchanger internal structure schematic diagram of the utility model embodiment 2;
Fig. 5 is middle super pressure-high temperature steam heating heat exchanger internal structure schematic diagram of the utility model embodiment 3;
Fig. 6 is middle super pressure-high temperature steam heating heat exchanger internal structure schematic diagram of the utility model embodiment 4;
Fig. 7 is middle super pressure-high temperature steam heating heat exchanger internal structure schematic diagram of the utility model embodiment 5;
Fig. 8-12 are the shape schematic diagram of radiating fin in the utility model;
Wherein, 1 is middle super pressure-high temperature pipe network, 2 is the first manually operated valve, 3 is filter screen, 4 is the second manually operated valve, 5 is gauge, 6 is thermometer, 7 is the first safety valve, 8 is the first pressure gauge, 9 is self-acting valve, 10 is the 3rd manually operated valve, 11 is smart valve, 12 is the second pressure gauge, 13 is middle super pressure-high temperature steam heating heat exchanger, 131 is heat conductive tube connection heat exchange sheet, 132 is heat conductive tube joining plate, 133 is end socket, 134 is suction flange, 135 is outlet(discharge) flange, 136 is dewatering outlet, 137 is support, 138 is radiating fin, 14 is single-phase valve, 15 is blowdown valve, 16 is reduction valve, 17 is automated intelligent valve, 18 is the 3rd pressure gauge, 19 is the second safety valve, 20 is drain valve, 21 is flash vessel.
Embodiment
Below in conjunction with specific embodiment, the utility model is further described, but protection domain of the present utility model is not limited to this.
embodiment 1
As shown in Figure 1, middle super pressure-high temperature steam control system of the present utility model, comprise middle super pressure-high temperature pipe network 1, middle super pressure-high temperature pipe network 1 is provided with the first manually operated valve 2 successively, filter screen 3, the second manually operated valve 4 and gauge 5, the both sides of gauge 5 are separately installed with the first safety valve 7 and thermometer 6, one side of the first safety valve 7 is provided with the first pressure gauge 8, the below of gauge 5 is provided with self-acting valve 9, self-acting valve 9 is arranged side by side 2, the below of self-acting valve 9 is provided with some heat-exchanging components, the below of heat-exchanging component is provided with reduction valve 16 and automated intelligent valve 17 successively, the both sides of automated intelligent valve 17 are separately installed with the 3rd pressure gauge 18 and drain valve 20, one side of the 3rd pressure gauge 18 is provided with the second safety valve 19, one side of the second safety valve 19 is connected with low temperature area, one side of drain valve 20 is connected with flash vessel 21 and common steam pipe network, heat-exchanging component one side and automated intelligent valve 17 belows are all provided with blowdown valve 15.
Heat-exchanging component in the utility model comprises the 3rd manually operated valve 10, smart valve 11, the second pressure gauge 12, middle super pressure-high temperature steam heating heat exchanger 13 and the single-phase valve 14 that are communicated with successively from top to bottom, and single-phase valve 14 is communicated with reduction valve 16.
As shown in Figures 2 and 3, middle super pressure-high temperature steam heating heat exchanger 13 in the utility model, comprise some heat conductive tube connection heat exchange sheets 131, heat conductive tube connection heat exchange sheet 131 is metal seamless heat conductive tube connection heat exchange sheet, can bear 30 kilograms of even larger pressure, also can bear high temperature, the outside of heat conductive tube connection heat exchange sheet 131 is coated with radiating fin 138, and the two ends of heat conductive tube connection heat exchange sheet 131 are all provided with heat conductive tube joining plate 132, heat conductive tube joining plate 132 outsides are provided with end socket 133, heat exchanger of the present utility model is also provided with suction flange 134, outlet(discharge) flange 135 and dewatering outlet 136, suction flange 134, outlet(discharge) flange 135 and dewatering outlet 136 are installed on end socket 133.
As shown in Fig. 8-12, the radiating fin 138 in the utility model can be circular, square, oval, semicircle or oval nest plate shape.When radiating fin 138 is circular, inside and outside being with radiating fin 138, heat conductive tube connection heat exchange sheet 131 is round shape; When radiating fin 138 is square, heat conductive tube connection heat exchange sheet 131 and radiating fin 138 are the shape of inner circle foreign side; When radiating fin 138 is oval, heat conductive tube connection heat exchange sheet 131 is inside and outside equal oval shape with radiating fin 138; When radiating fin 138 is semicircle, heat conductive tube connection heat exchange sheet 131 and radiating fin 138 are the shape of the outer semicircle of inner circle; When radiating fin 138 is oval nest plate shape, heat conductive tube connection heat exchange sheet 131 and radiating fin 138 are the shape of interior multiple oval foreign sides.When wherein radiating fin 138 is oval, radiating effect is best.
In the present embodiment 1, heat conductive tube connection heat exchange sheet 131 is tandem installation, suction flange 134 and outlet(discharge) flange 135 are arranged on respectively on two end sockets 133, dewatering outlet 136 is arranged on same end socket 133 with outlet(discharge) flange 135, and dewatering outlet 136 is positioned at outlet(discharge) flange 135 tops, and suction flange 134 is relative with dewatering outlet 136.
embodiment 2
As shown in Figure 4, in the present embodiment 2, some heat conductive tube connection heat exchange sheets 131 are parallel installation, suction flange 134, outlet(discharge) flange 135 and dewatering outlet 136 are arranged on same end socket 133, and suction flange 134 is positioned at the top of outlet(discharge) flange 135, and dewatering outlet 136 is arranged on the bottom of end socket 133.
Other structure and the Placement of the present embodiment 2 are identical with embodiment 1, do not repeat herein.
embodiment 3
As shown in Figure 5, middle super pressure-high temperature steam heating heat exchanger 13 in the present embodiment 3 is first horizontal, some heat conductive tube connection heat exchange sheets 131 are horizontal and arrange left and right, suction flange 134, outlet(discharge) flange 135 and dewatering outlet 136 are arranged on same end socket 133, and suction flange 134 is positioned at the top of outlet(discharge) flange 135, dewatering outlet 136 is arranged on the bottom of end socket 133.
Other structure and the Placement of the present embodiment 3 are identical with embodiment 1, do not repeat herein.
embodiment 4
As shown in Figure 6, middle super pressure-high temperature steam heating heat exchanger 13 in the present embodiment 4 is second horizontal, some heat conductive tube connection heat exchange sheets 131 are longitudinal and arrange left and right, suction flange 134 is arranged on same end socket 133 with outlet(discharge) flange 135, dewatering outlet 136 is arranged on different end socket 133 from outlet(discharge) flange 135, and outlet(discharge) flange 135 is relative with dewatering outlet 136.
Other structure and the Placement of the present embodiment 4 are identical with embodiment 1, do not repeat herein.
embodiment 5
As shown in Figure 7, middle super pressure-high temperature steam heating heat exchanger 13 in the present embodiment 5 is vertical, some heat conductive tube connection heat exchange sheets 131 are laterally and are arranged above and below, suction flange 134 is arranged on same end socket 133 with outlet(discharge) flange 135, suction flange 134 is positioned at outlet(discharge) flange 135 tops, dewatering outlet 136 is arranged on different end socket 133 from outlet(discharge) flange 135, and outlet(discharge) flange 135 is relative with dewatering outlet 136, heat conductive tube connection heat exchange sheet 131 outsides are provided with support 137, and support 137 two ends are all connected with heat conductive tube joining plate 132.
Other structure and the Placement of the present embodiment 5 are identical with embodiment 1, do not repeat herein.
When the utility model work, open the first manually operated valve 2, middle super pressure-high temperature steam therefrom enters in super pressure-high temperature pipe network 1, after filtering by filter screen 3, open the second manually operated valve 4, fall into a trap and measure the needed amount of reality in gauge 5, now can observe by thermometer 6 temperature of steam, observe the pressure of steam by the first pressure gauge 8, the vapor pressure excessive damage that cause system of the first safety valve 7 for preventing from entering, after the pressure and temperature of the to be determined steam needing, enter heat-exchanging component by self-acting valve 9, needed heat-exchanging component is several that install side by side, quantity can need to select according to actual industrial.Open the second manually operated valve 10, observe pressure by pressure gauge 12, smart valve 11 is controlled actual required pressure, and the steam of pressure controlled well enters middle super pressure-high temperature steam heating heat exchanger 13 and carries out heat exchange, then discharges by single-phase valve 14, and blowdown valve 15 is got rid of refuse.Pressure out in super pressure-high temperature steam heating heat exchanger 13 in first reducing by reduction valve 16 after access arrangement, automated intelligent valve 17 is according to temperature, the size of flow determines open or close, now from the 3rd pressure gauge 18, observe the pressure of steam, and ensured the Security of system by the second safety valve 19, steam now enters low temperature area, the water that system produces enters common steam pipe network by drain valve 20 or by removing other common steam equipment after flash vessel 21 flash distillations, last dirt is got rid of by blowdown valve, realize the steam heat-exchanging process that arranges, the demand of super pressure-high temperature in having met in industrial production, the waste water producing discharges by drain valve 20, can be applied in miscellaneous equipment, the waste gas producing is emitted on low temperature area by the second safety valve 19, realize the comprehensive utilization of the energy, be highly suitable for process hides tenter machine, hot pin spins the field application such as boarding machine.Super pressure-high temperature steam heating heat exchanger 13 in employing, can bear 30 kilograms of left and right, and pressure maximum is 36 kilograms, and temperature can reach 320 DEG C, can meet the needs of the middle super pressure-high temperature of needs in industrial production.Adopt steam heating; can adopt industrial exhaust heat steam as heat exchange source; realize step UTILIZATION OF VESIDUAL HEAT IN; very large contribution is made in the utilization that is not only new energy, and has effectively avoided the haze in boiler burning, has eliminated the source of haze; consistent with the theme of environmental protection; and low price, cost is low, simple to operate.Heat conductive tube connection heat exchange sheet outside is coated with the radiating fin of circle, square, oval, semicircle or oval nest plate shape, and radiating effect is very good.And middle super pressure-high temperature steam heating heat exchanger 13 can become tandem, parallel, first horizontal, second horizontal or vertical according to the different Demand Design of commercial Application, meets the arrangement of different industrial production systems.
In the utility model, be provided with reduction valve 16, the pressure in reducing according to actual needs in super pressure-high temperature steam heating heat exchanger 13, protects follow-up equipment.Whether the automated intelligent valve 17 arranging can determine closure or openness according to temperature, flow, and not only loss is little, more energy-conservation, has also increased the working life of middle super pressure-high temperature steam heating heat exchanger 13.
Above-described embodiment is only for the inventive concept of the present utility model of explaining; but not restriction to the utility model rights protection; as allly in change of suction flange 4, outlet(discharge) flange 5 and dewatering outlet 6 mounting point in end socket 3 etc. utilize this design to carry out the change of unsubstantiality to the utility model; all should fall into protection domain of the present utility model, in all the utility model, not have the structure and the Placement that occur to be the known property general knowledge of related domain.
Claims (10)
1. super pressure-high temperature steam control system in a kind, it is characterized in that: comprise middle super pressure-high temperature pipe network, described middle super pressure-high temperature pipe network is provided with the first manually operated valve successively, filter screen, the second manually operated valve and gauge, the both sides of described gauge are separately installed with the first safety valve and thermometer, one side of described the first safety valve is provided with the first pressure gauge, the below of described gauge is provided with self-acting valve, the below of described self-acting valve is provided with some heat-exchanging components, the below of described heat-exchanging component is provided with reduction valve and automated intelligent valve successively, the both sides of described automated intelligent valve are separately installed with the 3rd pressure gauge and drain valve, described a 3rd manometric side is provided with the second safety valve, one side of described the second safety valve is connected with low temperature area, one side of described drain valve is connected with flash vessel and common steam pipe network, described heat-exchanging component one side and automated intelligent valve below are all provided with blowdown valve, described heat-exchanging component comprises the 3rd manually operated valve, smart valve, the second pressure gauge, middle super pressure-high temperature steam heating heat exchanger and the single-phase valve that are communicated with successively from top to bottom, and described single-phase valve is communicated with reduction valve.
2. middle super pressure-high temperature steam control system as claimed in claim 1, it is characterized in that: described middle super pressure-high temperature steam heating heat exchanger comprises some heat conductive tube connection heat exchange sheets, described heat conductive tube connection heat exchange sheet is metal seamless heat conductive tube connection heat exchange sheet, the outside of heat conductive tube connection heat exchange sheet is coated with radiating fin, and the two ends of heat conductive tube connection heat exchange sheet are all provided with heat conductive tube joining plate, described heat conductive tube joining plate outside is provided with end socket, described heat exchanger is also provided with suction flange, outlet(discharge) flange and dewatering outlet, described suction flange, outlet(discharge) flange and dewatering outlet are installed on end socket.
3. middle super pressure-high temperature steam control system as claimed in claim 2, it is characterized in that: described some heat conductive tube connection heat exchange sheets are that tandem is installed, described suction flange and outlet(discharge) flange are arranged on respectively on two end sockets, described dewatering outlet and outlet(discharge) flange are arranged on same end socket, and dewatering outlet is positioned at outlet(discharge) flange top, and suction flange is relative with dewatering outlet.
4. middle super pressure-high temperature steam control system as claimed in claim 2, it is characterized in that: described some heat conductive tube connection heat exchange sheets are parallel installation, described suction flange, outlet(discharge) flange and dewatering outlet is arranged on same end socket, and suction flange is positioned at the top of outlet(discharge) flange, dewatering outlet is arranged on the bottom of end socket.
5. middle super pressure-high temperature steam control system as claimed in claim 2, it is characterized in that: described heat exchanger is first horizontal, described some heat conductive tube connection heat exchange sheets are horizontal and arrange left and right, described suction flange, outlet(discharge) flange and dewatering outlet is arranged on same end socket, and suction flange is positioned at the top of outlet(discharge) flange, dewatering outlet is arranged on the bottom of end socket.
6. middle super pressure-high temperature steam control system as claimed in claim 2, it is characterized in that: described heat exchanger is second horizontal, described some heat conductive tube connection heat exchange sheets are longitudinal and arrange left and right, described suction flange and outlet(discharge) flange are arranged on same end socket, described dewatering outlet is arranged on different end sockets from outlet(discharge) flange, and outlet(discharge) flange is relative with dewatering outlet.
7. middle super pressure-high temperature steam control system as claimed in claim 2, it is characterized in that: described heat exchanger is vertical, described some heat conductive tube connection heat exchange sheets are laterally and are arranged above and below, described suction flange and outlet(discharge) flange are arranged on same end socket, suction flange is positioned at outlet(discharge) flange top, described dewatering outlet is arranged on different end sockets from outlet(discharge) flange, and outlet(discharge) flange is relative with dewatering outlet, described heat conductive tube connection heat exchange sheet outside is provided with support, and described support two ends are all connected with heat conductive tube joining plate.
8. the middle super pressure-high temperature steam control system as described in claim as arbitrary in claim 2-7, is characterized in that: described radiating fin is circular, square, oval, semicircle or oval nest plate shape.
9. middle super pressure-high temperature steam control system as claimed in claim 8, is characterized in that: described radiating fin is for oval.
10. middle super pressure-high temperature steam control system as claimed in claim 1, is characterized in that: described self-acting valve is arranged side by side 2.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420180576.6U CN203907225U (en) | 2014-04-14 | 2014-04-14 | Medium pressure high temperature steam control system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420180576.6U CN203907225U (en) | 2014-04-14 | 2014-04-14 | Medium pressure high temperature steam control system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203907225U true CN203907225U (en) | 2014-10-29 |
Family
ID=51781503
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420180576.6U Expired - Fee Related CN203907225U (en) | 2014-04-14 | 2014-04-14 | Medium pressure high temperature steam control system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203907225U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103953851A (en) * | 2014-04-14 | 2014-07-30 | 浙江精宝机械有限公司 | Medium-pressure high-temperature steam control system |
| CN103953851B (en) * | 2014-04-14 | 2016-11-30 | 浙江精宝机械有限公司 | Middle super pressure-high temperature steam control system |
| CN109443076A (en) * | 2017-11-26 | 2019-03-08 | 上海电气电站环保工程有限公司 | Long-range control method, system, electric terminal, medium and heat-exchanger rig |
| CN109827072A (en) * | 2019-01-23 | 2019-05-31 | 新奥数能科技有限公司 | The control method and server of steam pipe network system |
-
2014
- 2014-04-14 CN CN201420180576.6U patent/CN203907225U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103953851A (en) * | 2014-04-14 | 2014-07-30 | 浙江精宝机械有限公司 | Medium-pressure high-temperature steam control system |
| CN103953851B (en) * | 2014-04-14 | 2016-11-30 | 浙江精宝机械有限公司 | Middle super pressure-high temperature steam control system |
| CN109443076A (en) * | 2017-11-26 | 2019-03-08 | 上海电气电站环保工程有限公司 | Long-range control method, system, electric terminal, medium and heat-exchanger rig |
| CN109827072A (en) * | 2019-01-23 | 2019-05-31 | 新奥数能科技有限公司 | The control method and server of steam pipe network system |
| CN109827072B (en) * | 2019-01-23 | 2021-09-14 | 新奥数能科技有限公司 | Control method and server of steam pipe network system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| EP2921272A1 (en) | Pump-type autoclave system and steam and pressure supply method thereof | |
| CN201915124U (en) | Annealing furnace waste heat recovery system | |
| CN203907225U (en) | Medium pressure high temperature steam control system | |
| US9579820B2 (en) | Solar autoclave equipment | |
| US10502456B2 (en) | Efficient solar flat plate heat absorption system and operation method thereof | |
| CN104406144A (en) | Double-medium waste heat boiler | |
| CN204482848U (en) | Noodle producing line solar drying system | |
| CN103968366A (en) | Biomass boiler blow-down waste heat recycling system | |
| CN103953851A (en) | Medium-pressure high-temperature steam control system | |
| CN203837525U (en) | Medium pressure and high temperature steam heating heat exchanger | |
| CN204388656U (en) | A kind of heat exchanger | |
| CN103953851B (en) | Middle super pressure-high temperature steam control system | |
| CN204268935U (en) | Energy-saving steam-water plate heat exchanger unit | |
| CN202008309U (en) | Condenser for heating | |
| CN205383588U (en) | Exhaust -heat boiler water heater that condenses | |
| CN204717661U (en) | A kind of industrial combustion gas steam generator system | |
| CN212081211U (en) | Boiler sampling heat energy recycling system | |
| CN203785229U (en) | Gas water heater | |
| CN204301021U (en) | Flue gas waste heat recovery apparatus | |
| CN204648205U (en) | Steam power plant's back-end ductwork is without pump self-loopa two-way water feeding high/low temperature associating heating system | |
| CN203147734U (en) | Thermal power plant flue gas waste heat recovery device | |
| CN215765727U (en) | Multi-channel pipeline heating and exhausting structure | |
| CN104560584A (en) | Energy-saving tube nest heat exchanger for steaming grains and energy-saving white spirit brewing system | |
| CN204730515U (en) | Complex energy recycling system in a kind of region realizing the utilization of energy ladder | |
| CN202647696U (en) | Off-machine coater heat supply recycling operation system |
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: 20141029 Termination date: 20190414 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |