CN212157112U - Temperature control circulating system - Google Patents
Temperature control circulating system Download PDFInfo
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- CN212157112U CN212157112U CN202020807073.2U CN202020807073U CN212157112U CN 212157112 U CN212157112 U CN 212157112U CN 202020807073 U CN202020807073 U CN 202020807073U CN 212157112 U CN212157112 U CN 212157112U
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Abstract
The utility model discloses a temperature control circulation system, which comprises a condensate water recovery machine, a water tank, a temperature control production line, a first boiler, a second boiler and a branch cylinder, wherein the upper end of the condensate water recovery machine is provided with a water inlet, one side of the water inlet is provided with a gas outlet, the other side is respectively provided with a safety valve interface, a pressure gauge interface and an outside workshop gas interface, the lower end of the condensate water recovery machine is provided with a sewage outlet and a first return port, the machine body of the condensate water recovery machine is provided with a second return port and a thermometer, the first return port is connected with the water tank through a condensate water circulating pipe, one end of the condensate water circulating pipe close to the first return port is provided with a first water replenishing pump, the condensate water circulating pipe is respectively connected with the first boiler and the second boiler through branch pipes, the first boiler and the second boiler, the branch cylinder is connected with a temperature control production line through a second air inlet main pipeline, and a water return pipe is arranged on the temperature control production line.
Description
Technical Field
The utility model relates to a temperature control system, specific theory, especially, control by temperature change circulation system.
Background
The environmental protection gets into the production of mill gradually, and the natural gas boiler must successive change in the packing trade, and traditional comdenstion water is retrieved the machine and can not use the natural gas boiler synchronous, leads to the natural gas boiler can not retrieve the comdenstion water to lose a large amount of heats, be not conform to the environmental protection production concept of current implementation.
SUMMERY OF THE UTILITY MODEL
The utility model aims at providing an energy-concerving and environment-protective, the fast control by temperature change circulation system of boiler programming rate to solve the problem that proposes in the above-mentioned background art.
The technical scheme of the utility model is realized like this: a temperature control circulating system comprises a condensate water recycling machine, a water tank, a temperature control production line, a first boiler, a second boiler and a branch cylinder, wherein a water inlet is formed in the upper end of the condensate water recycling machine, an air outlet is formed in one side of the water inlet, a safety valve interface, a pressure gauge interface and a workshop external exhaust interface are respectively formed in the other side of the condensate water recycling machine, a sewage discharge outlet and a first water return outlet are formed in the lower end of the condensate water recycling machine, a second water return outlet and a thermometer are formed in the machine body of the condensate water recycling machine, the first water return outlet is connected with the water tank through a condensate water circulating pipe, a first water replenishing pump is installed at one end, close to the first water return outlet, of the condensate water circulating pipe, the condensate water circulating pipe is respectively connected with the first boiler and the second boiler through branch pipes, the first boiler and the second boiler are connected, and a water return pipe is arranged on the temperature control production line, the water return pipe is communicated with the water inlet, and the second water return port is communicated with the water tank through a second water replenishing pump.
In the temperature control circulation system, the safety valve interface is connected with the condensed water circulation pipe through the first pipeline.
In the temperature control circulation system, the air outlet is communicated with the water tank through a pressure loop pipe, and a pneumatic valve is arranged on the pressure loop pipe.
In the temperature control circulating system, a manual high-temperature ball valve is arranged at one end, close to the water inlet, of the water return pipe.
In the temperature control circulation system, the safety valve interface is communicated with the condensed water circulation pipe through the condensed water branch pipe, and the condensed water branch pipe is provided with the manual high-temperature ball valve.
In the temperature control circulation system, one end of the condensed water circulation pipe close to the first water replenishing pump is communicated with the water tank through a water replenishing pipe.
The beneficial effects of the utility model reside in that: the utility model uses the first return port of the condensate water recovery machine to convey the condensate water which is difficult to be utilized into the return water tank through the condensate water circulating pipe, then the water tank is connected with the second return port through the second water replenishing pump, thereby the water in the water tank can be conveyed into the condensate water recovery machine, and the condensate water circulating pipe is respectively connected with the first boiler and the second boiler through the branch pipes, thereby the condensate water is conveyed to the first boiler and the second boiler to be heated and evaporated at high temperature, the high-temperature steam is conveyed to the temperature control production line through the branch cylinder to be used, in the using process, the high-temperature steam is changed into the condensate water to be returned to the water tank through the return water pipe to be reused again, and the temperature of the condensate water in the water tank is raised, in the recycling process, the condensate water loss is less, the heat energy loss of the water can be reduced, the, the energy-saving effect is achieved.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
In the figure: the system comprises a condensate water recycling machine 1, a water inlet 2, a gas outlet 3, a safety valve interface 4, a pressure gauge interface 5, an exhaust interface 6 outside a workshop, a second water return port 7, a sewage discharge port 8, a first water return port 9, a thermometer 10, a water tank 11, a temperature control production line 12, a first boiler 13, a second boiler 14, a first water replenishing pump 15, a condensate water circulating pipe 16, a water replenishing pipe 17, a first main air inlet pipe 18, a manual high-temperature ball valve 19, a branch air cylinder 20, a second main air inlet pipe 21, a water return pipe 22, a pressure loop pipe 23, a second water replenishing pump 24, a condensate water branch pipe 25 and a pneumatic valve 26.
Detailed Description
The claimed technical solution of the present invention will now be described in further detail with reference to the accompanying drawings and specific embodiments.
As shown in fig. 1, a temperature control circulation system includes a condensate water recycling machine 1, a water tank 11, a temperature control production line 12, a first boiler 13, a second boiler 14 and a branch cylinder 20, wherein a water inlet 2 is arranged at the upper end of the condensate water recycling machine 1, an air outlet 3 is arranged at one side of the water inlet 2, a safety valve interface 4, a pressure gauge interface 5 and an air outlet interface 6 outside a workshop are respectively arranged at the other side of the water inlet 2, a drain outlet 8 and a first water return outlet 9 are arranged at the lower end of the condensate water recycling machine 1, a drain pipe is arranged on the drain outlet 8, a second water return outlet 7 and a thermometer 10 are arranged on the machine body of the condensate water recycling machine 1, the first water return outlet 9 is connected with the water tank 11 through a condensate water circulation pipe 16, a first water replenishing pump 15 is arranged at one end of the condensate water circulation pipe 16 close, The second boiler 14 is connected, first boiler 13 and second boiler 14 are connected with branch cylinder 20 through first inlet main pipeline 18, branch cylinder 20 is connected with control by temperature change production line 12 through second inlet main pipeline 21, be equipped with wet return 22 on the control by temperature change production line 12, wet return 22 is linked together with water inlet 2, second return mouth 7 is linked together with water tank 11 through second moisturizing pump 24.
The safety valve interface 4 is connected with a condensed water circulating pipe 16 through a first pipeline, the air outlet 3 is communicated with the water tank 11 through a pressure loop pipe 23, a pneumatic valve 26 is arranged on the pressure loop pipe 23, a manual high-temperature ball valve 19 is arranged at one end, close to the water inlet 2, of the water return pipe 22, the safety valve interface 4 is communicated with the condensed water circulating pipe 16 through a condensed water branch pipe 25, the manual high-temperature ball valve is arranged on the condensed water branch pipe 25, and one end, close to the first water replenishing pump 15, of the condensed water circulating pipe 16 is communicated with the water tank 11 through a water replenishing pipe 17.
The utility model discloses a first return opening 9 of condensate water recovery machine 1 carries the return water tank 11 through the comdenstion water circulating pipe 16 in the comdenstion water that will be difficult to utilize, then water tank 11 is connected with second return opening 7 through second moisturizing pump 24, thereby can carry the water in the water tank 11 in condensate water recovery machine 1, and on the comdenstion water circulating pipe 16 respectively through the bleeder pipe with first boiler 13, second boiler 14 is connected, thereby carry the comdenstion water to first boiler 13, second boiler 14 carries out the high temperature heating evaporation, carry high temperature steam through cylinder 20 and control by temperature change production line 12 and use, in the use, high temperature steam turns back the comdenstion water and returns water tank 11 through return pipe 22 and used repeatedly once more, and make the comdenstion water temperature rise in the water tank 11, in the recycling process, the comdenstion water that runs off is less, can reduce the heat energy loss of water, the heating speed of the boiler is increased, so that the fuel consumption and the water replenishing times are reduced, and the energy-saving effect is achieved.
Furthermore, it should be understood that although the present description refers to embodiments, not every embodiment may contain only a single embodiment, and such description is for clarity only, and those skilled in the art should integrate the description, and the embodiments may be combined as appropriate to form other embodiments understood by those skilled in the art.
Claims (6)
1. A temperature control circulating system comprises a condensate water recycling machine (1), a water tank (11), a temperature control production line (12), a first boiler (13), a second boiler (14) and a branch cylinder (20), and is characterized in that a water inlet (2) is arranged at the upper end of the condensate water recycling machine (1), a gas outlet (3) is arranged on one side of the water inlet (2), a safety valve interface (4), a pressure gauge interface (5) and an exhaust interface (6) outside a workshop are respectively arranged on the other side of the condensate water recycling machine, a sewage discharge port (8) and a first water return port (9) are arranged at the lower end of the condensate water recycling machine (1), a second water return port (7) and a thermometer (10) are arranged on a machine body of the condensate water recycling machine (1), the first water return port (9) is connected with the water tank (11) through a condensate water circulating pipe (16), and a first water replenishing pump (15) is, the condensed water circulating pipe (16) is connected with a first boiler (13) and a second boiler (14) through branch pipes respectively, the first boiler (13) and the second boiler (14) are connected with a branch cylinder (20) through a first air inlet main pipeline (18), the branch cylinder (20) is connected with a temperature control production line (12) through a second air inlet main pipeline (21), a water return pipe (22) is arranged on the temperature control production line (12), the water return pipe (22) is communicated with a water inlet (2), and a second water return port (7) is communicated with a water tank (11) through a second water replenishing pump (24).
2. The thermostatted cycle system as claimed in claim 1, characterized in that the safety valve port (4) is connected to a condensate recirculation line (16) via a first line.
3. A temperature controlled circulation system according to claim 1, wherein the outlet (3) communicates with the tank (11) via a pressure loop (23), the pressure loop (23) being provided with a pneumatic valve (26).
4. Temperature-controlled circulation system according to claim 1, characterized in that the return pipe (22) is provided with a manual high-temperature ball valve (19) at its end near the water inlet (2).
5. A temperature controlled circulation system according to claim 1, wherein the safety valve port (4) communicates with the condensate circulating pipe (16) via a condensate branch pipe (25), the condensate branch pipe (25) being provided with a manual high temperature ball valve.
6. A temperature controlled circulation system according to claim 1 wherein the end of the condensate circulating pipe (16) adjacent the first make-up pump (15) is connected to the water tank (11) by a make-up pipe (17).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020807073.2U CN212157112U (en) | 2020-05-15 | 2020-05-15 | Temperature control circulating system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020807073.2U CN212157112U (en) | 2020-05-15 | 2020-05-15 | Temperature control circulating system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN212157112U true CN212157112U (en) | 2020-12-15 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202020807073.2U Active CN212157112U (en) | 2020-05-15 | 2020-05-15 | Temperature control circulating system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN212157112U (en) |
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2020
- 2020-05-15 CN CN202020807073.2U patent/CN212157112U/en active Active
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210506 Address after: 528200 12 / 3 hegui Avenue, Heshun hegui Industrial Park, Lishui Town, Nanhai District, Foshan City, Guangdong Province Patentee after: Guangdong Fengyuan Machinery Technology Co.,Ltd. Address before: 528200 Heshun hegui Industrial Park, Lishui Town, Nanhai District, Foshan City, Guangdong Province Patentee before: FOSHAN FENGYUAN MACHINERY Co.,Ltd. |