CN116045265A - Mechanical compression type steam generation system - Google Patents
Mechanical compression type steam generation system Download PDFInfo
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- CN116045265A CN116045265A CN202211726764.XA CN202211726764A CN116045265A CN 116045265 A CN116045265 A CN 116045265A CN 202211726764 A CN202211726764 A CN 202211726764A CN 116045265 A CN116045265 A CN 116045265A
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- 238000007906 compression Methods 0.000 title claims abstract description 32
- 230000006835 compression Effects 0.000 title claims abstract description 32
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 109
- 239000007788 liquid Substances 0.000 claims abstract description 89
- 230000001502 supplementing effect Effects 0.000 claims abstract description 50
- 238000005507 spraying Methods 0.000 claims abstract description 45
- 238000007599 discharging Methods 0.000 claims abstract description 6
- 239000007921 spray Substances 0.000 claims description 34
- 238000005485 electric heating Methods 0.000 abstract description 17
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 230000006872 improvement Effects 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 9
- 230000005484 gravity Effects 0.000 description 6
- 238000000926 separation method Methods 0.000 description 6
- 238000012544 monitoring process Methods 0.000 description 5
- 230000001105 regulatory effect Effects 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000003595 mist Substances 0.000 description 3
- 230000008016 vaporization Effects 0.000 description 3
- 239000002028 Biomass Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 230000002950 deficient Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 238000012994 industrial processing Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
Images
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/28—Methods of steam generation characterised by form of heating method in boilers heated electrically
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B37/00—Component parts or details of steam boilers
- F22B37/02—Component parts or details of steam boilers applicable to more than one kind or type of steam boiler
- F22B37/26—Steam-separating arrangements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B37/00—Component parts or details of steam boilers
- F22B37/78—Adaptations or mounting of level indicators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22D—PREHEATING, OR ACCUMULATING PREHEATED, FEED-WATER FOR STEAM GENERATION; FEED-WATER SUPPLY FOR STEAM GENERATION; CONTROLLING WATER LEVEL FOR STEAM GENERATION; AUXILIARY DEVICES FOR PROMOTING WATER CIRCULATION WITHIN STEAM BOILERS
- F22D11/00—Feed-water supply not provided for in other main groups
- F22D11/02—Arrangements of feed-water pumps
- F22D11/06—Arrangements of feed-water pumps for returning condensate to boiler
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F25/00—Component parts of trickle coolers
- F28F25/02—Component parts of trickle coolers for distributing, circulating, and accumulating liquid
- F28F25/06—Spray nozzles or spray pipes
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Water Supply & Treatment (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention discloses a mechanical compression type steam generation system, which mainly comprises parts of water supplementing, spraying, water spraying, compression, steam discharging, liquid returning, steam supplying and the like; the water supplementing, spraying, water spraying, compressing and liquid returning parts are connected with each other, the water spraying is connected with the compressing part, the compressing and steam discharging part is connected, the compressing and liquid returning parts are connected, and the steam discharging, liquid returning and steam supplying parts are connected with each other. Compared with an electric heating steam generator, the system obtains low-temperature steam through electric heating in the early stage, and generates high-temperature steam through mechanical compression of the low-temperature steam in the later stage, only a small part of electric energy is consumed to circularly improve the temperature, pressure and heat value of the steam, the efficiency of steam generation is improved, the consumption of electric energy is reduced, the further energy-saving improvement of the electric heating steam generator is realized, and the system has the advantages of low operation cost, high efficiency, energy saving, safety, environmental protection, clean energy and the like; the system is very suitable for the steam supply requirement of the steam range of 100-170 ℃.
Description
Technical Field
The invention belongs to the field of steam heat supply, and particularly relates to a mechanical compression type steam generation system.
Background
The steam generator is also called a steam boiler/steam heat source machine/steam generation system, and is an essential steam supply device in the industrial production and processing process. The fuel can be divided into an electric heating steam generator, a fuel gas steam generator, a fuel oil steam generator and a biomass steam generator. As the national requirements for environmental protection become higher, the use of coal-fired boilers has been banned in most areas. Because of the pollution emission of biomass and fuel combustion, the method is only suitable for remote towns or rural areas, but eventually can be forbidden. At present, a gas steam generator and an electric heating steam generator are mainly used, but the gas steam generator is limited by gas connection and insufficient gas, and particularly, the problem of peak use occurs; the electric heating steam generator only completely meets the requirements of energy green development in recent years, but is also limited by the power consumption of enterprises, so that the energy conservation and emission reduction of the electric heating steam generator are urgent.
CN201059543Y provides an energy-saving heat pump type steam generator, which heats cold water by a heat pump unit to obtain low-temperature hot water, and then sends the low-temperature hot water to an electric energy heater for secondary heating, thereby generating high-temperature and high-pressure steam; the patent mainly utilizes a heat pump unit to prepare low-temperature hot water for energy saving. CN114643637a provides a prefabricated case roof beam steam generation system for health preserving, has solved current spray distance and has not fixed, sprays the homogeneity poor, influences technical problem such as maintenance quality. CN213077522U and CN207822537U both provide a vapor generator built-in to the MVR evaporator, CN213077522U improves the efficiency of the output of vapor to the MVR evaporator, and CN207822537U has an integrated design for the vapor generator and MVR evaporator, both of which are devices for assisting the MVR evaporator to generate vapor. The steam generating systems of all of the above patents are quite different from the present invention, with obvious differences.
From the technical and economic point of view, the invention provides a mechanical compression type steam generation system, which obtains low-temperature steam by using electric heating in the previous stage, and generates high-temperature steam by mechanically compressing the low-temperature steam in the later stage, and circularly improves the temperature, pressure and heat value of the steam by consuming less electric energy so as to improve the steam generation efficiency of the system and reduce the electric energy consumption at the same time; the system has important significance for the current environment-friendly energy-saving policy.
Disclosure of Invention
First, the technical problem to be solved
The technical problems to be solved by the invention are as follows: overcomes the defects existing in the prior art, and provides a mechanical compression type steam generation system for improving the steam generation efficiency of an electric heating steam generator, reducing the consumption of electric energy and the operation cost, realizing high efficiency and energy saving.
(II) technical scheme
In order to solve the technical problems, the technical scheme of the invention is as follows: a mechanical compression type steam generation system mainly comprises parts of water supplementing, spraying, water spraying, compression, steam discharging, liquid returning, steam supplying and the like; the water replenishing, spraying, water spraying, compressing and liquid returning parts are connected with each other and are crossed with the separator (FLQ); the water spray and compression section are connected and intersect a compressor (YSJ); the compression and exhaust sections are connected and intersect with an exhaust valve (PQF); the compression part and the liquid return part are connected and are intersected with the rotational flow inlet 1 (XLJ 1); the steam exhaust, liquid return and steam supply parts are mutually connected and are intersected with the steam supplementing tank (BQG).
Further, the water supplementing part comprises a water supplementing source (BSY), a water supplementing pump (BSB), a water supplementing valve (BSF) and a separator (FLQ) which are connected in sequence;
the water supplementing pump (BSB) is used for supplementing the suction of a water source (BSY);
the make-up valve (BSF) is used to regulate the make-up water flow to the separator (FLQ);
the separator (FLQ) is provided with a liquid level gauge 1 (LWJ 1) for monitoring and regulating the make-up flow and the return flow;
the separator (FLQ) is provided with electric heating (DJR) for heating liquid water therein to generate low-temperature water vapor.
Further, the spraying part comprises a separator (FLQ), a spraying Pump (PLB), a spraying valve (PLF) and a separator (FLQ) which are connected in sequence;
the separator (FLQ) is provided with a mist spraying device for quickly vaporizing liquid water to generate more water vapor;
the spray Pump (PLB) is used for sucking spray liquid;
the spray valve (PLF) is used to regulate the flow of spray water to the separator (FLQ).
Further, the water spraying part comprises a separator (FLQ), a water spraying Pump (PSB), a water spraying valve (PSF) and a compressor (YSJ) which are connected in sequence;
the spray Pump (PSB) is used for sucking water spray;
the water spray valve (PSF) is used to regulate the water spray flow to the compressor (YSJ).
Further, the compression part comprises a separator (FLQ), a liquid remover (CYQ), a compressor (YSJ), a circulating valve (XHF), a rotational flow inlet 1 (XLJ 1) and a separator (FLQ) which are connected in sequence;
-the liquid separator (CYQ) is used for removing liquid entrained in the vaporized water vapor in the separator (FLQ);
the compressor (YSJ) may be a water vapor compressor in the form of roots, screws, centrifugation, or the like;
-the circulation valve (XHF) is used to turn on or off the compressed steam flowing to the separator (FLQ);
the cyclone inlet 1 (XLJ 1) is used for cyclone gravity separation of gas and liquid.
Further, the steam exhaust part comprises a compressor (YSJ), a steam exhaust valve (PQF), a one-way valve (DXF), a rotational flow inlet 2 (XLJ 2) and a steam supplementing tank (BQG) which are connected in sequence;
the exhaust valve (PQF) is used for opening or closing the compressed steam flowing to the steam supplementing tank (BQG);
the check valve (DXF) is used for preventing the steam inside the steam supplementing tank (BQG) from flowing backwards;
the cyclone inlet 2 (XLJ 2) is used for cyclone gravity separation of gas and liquid;
the make-up tank (BQG) is for storing compressed steam from a compressor (YSJ).
Further, the liquid return part comprises a vapor supplementing tank (BQG), a liquid return valve (HYF), a liquid return pump (HYB), a rotational flow inlet 1 (XLJ 1) and a separator (FLQ) which are connected in sequence;
the steam supplementing tank (BQG) is provided with a liquid level meter 2 (LWJ 2) for monitoring and adjusting the liquid level;
the liquid return valve (HYF) is used for adjusting the liquid return flow rate flowing to the separator (FLQ);
the liquid return pump (HYB) is used for sucking the liquid return.
Further, the steam supply part comprises a steam supplementing tank (BQG) and a steam valve (ZQF) which are connected in sequence;
the steam valve (ZQF) is used to regulate the flow of steam to the outside of the system.
(III) beneficial effects
After the technical scheme is adopted, the invention has the following beneficial effects:
(1) Compared with an electric heating steam generator, the system obtains low-temperature steam through electric heating in the early stage, and generates high-temperature steam through mechanical compression of the low-temperature steam in the later stage, only a small part of electric energy is consumed to circularly improve the temperature, pressure and heat value of the steam, the efficiency of generating the steam is greatly improved, the consumption of the electric energy is greatly reduced, the operation cost is lower, and the energy-saving effect is more remarkable;
(2) The system realizes further energy-saving improvement on the electric heating steam generator and has the advantages of low operation cost, high efficiency, energy saving, safety, environmental protection, clean energy and the like;
(3) The system is very suitable for the steam supply requirement of the steam range of 100-170 ℃.
Drawings
In order to more clearly illustrate the embodiments of the invention or the technical solutions in the prior art, the drawings that are required in the embodiments or the description of the prior art will be briefly described, it being obvious that the drawings in the following description are only some embodiments of the invention, and that other drawings may be obtained according to these drawings without inventive effort for a person skilled in the art.
Fig. 1 is a mechanical compression type steam generation system of the present invention.
The symbols in the figures are respectively as follows:
a water supplementing source (BSY), a water supplementing pump (BSB), a water supplementing valve (BSF), a separator (FLQ), a liquid level meter 1 (LWJ 1), an electric heater (DJR), a spray Pump (PLB), a spray valve (PLF), a spray Pump (PSB), a spray valve (PSF), a liquid remover (CYQ), a compressor (YSJ), a circulation valve (XHF), a swirl inlet 1 (XLJ 1), a steam exhausting valve (PQF), a one-way valve (DXF), a swirl inlet 2 (XLJ 2), a steam supplementing tank (BQG), a steam valve (ZQF), a liquid level meter 2 (LWJ 2), a liquid return valve (HYF), and a liquid return pump (HYB).
Detailed Description
In order that the invention may be more readily understood, a more particular description of the invention will be rendered by reference to specific embodiments that are illustrated in the appended drawings.
As shown in figure 1, the mechanical compression type steam generation system mainly comprises parts such as water supplementing, spraying, water spraying, compression, steam discharging, liquid returning, steam supplying and the like;
the water replenishing, spraying, water spraying, compressing and liquid returning parts are connected with each other and are crossed with the separator (FLQ);
the water spray and compression section are connected and intersect a compressor (YSJ);
the compression and exhaust sections are connected and intersect with an exhaust valve (PQF);
the compression part and the liquid return part are connected and are intersected with the rotational flow inlet 1 (XLJ 1);
the steam exhaust, liquid return and steam supply parts are mutually connected and are intersected with the steam supplementing tank (BQG).
Preferably, as shown in fig. 1, the water replenishing part comprises a water replenishing source (BSY), a water replenishing pump (BSB), a water replenishing valve (BSF) and a separator (FLQ) which are connected in sequence, and the water replenishing part is used for realizing the water replenishing function of the system;
the water supplementing pump (BSB) is used for supplementing the suction of a water source (BSY);
the make-up valve (BSF) is used to regulate the make-up water flow to the separator (FLQ);
the separator (FLQ) is provided with a liquid level gauge 1 (LWJ 1) for monitoring and regulating the make-up flow and the return flow;
the separator (FLQ) is provided with electric heating (DJR) for heating liquid water in the separator to generate low-temperature water vapor;
the work flow of the water supplementing part is specifically as follows:
firstly, a water supplementing valve (BSF) is opened, a water supplementing pump (BSB) is started to send liquid water from a water supplementing source (BSY) into a separator (FLQ); secondly, controlling the water supplementing process through a liquid level meter 1 (LWJ 1) arranged on the separator (FLQ); then, the liquid water in the separator (FLQ) is heated by electric heating (DJR) to generate low-temperature water vapor; and finally, starting the water supplementing function when water is deficient, and closing the water supplementing function when water is not deficient, thereby completing the whole water supplementing working cycle.
Preferably, as shown in fig. 1, the spraying part comprises a separator (FLQ), a spraying Pump (PLB), a spraying valve (PLF) and a separator (FLQ) which are connected in sequence, and the spraying part is used for realizing a spraying function of closed circulation of spraying liquid;
the separator (FLQ) is provided with a mist spraying device for quickly vaporizing liquid water to generate more water vapor;
the spray Pump (PLB) is used for sucking spray liquid;
the spray valve (PLF) is used for adjusting the flow rate of spray water flowing to the separator (FLQ);
the working flow of the spraying part is specifically as follows:
firstly, high-temperature liquid water heated by electric heating (DJR) in a separator (FLQ) flows to a spray Pump (PLB); secondly, a spray valve (PLF) is opened and regulated, high-temperature liquid water is sent into a separator (FLQ) to be sprayed in a mist form from top to bottom, and the high-temperature liquid water exchanges heat with high-temperature gaseous steam from a rotational flow inlet 1 (XLJ 1) from bottom to top to be partially vaporized and finally flows to a liquid remover (CYQ); finally, the spraying function of the spraying liquid is realized by continuously carrying out closed circulation spraying, so that the whole spraying working cycle is completed.
Preferably, as shown in fig. 1, the water spraying part includes a separator (FLQ), a water spraying Pump (PSB), a water spraying valve (PSF), a compressor (YSJ) connected in sequence for implementing a water spraying function of the compressor (YSJ);
the spray Pump (PSB) is used for sucking water spray;
the water spray valve (PSF) is used for adjusting the water spray flow rate to the compressor (YSJ);
the working flow of the water spraying part is specifically as follows:
firstly, high-temperature liquid water heated by electric heating (DJR) in a separator (FLQ) flows to a water spraying Pump (PSB); secondly, opening and adjusting a water spray valve (PSF), feeding high-temperature liquid water into a compressor (YSJ) for reducing the superheat degree of compressed steam and for sealing a compression cavity; finally, the excess liquid water re-enters the separator (FLQ) with the compressed portion, thereby completing the entire water spray cycle.
Preferably, as shown in fig. 1, the compression part comprises a separator (FLQ), a liquid separator (CYQ), a compressor (YSJ), a circulation valve (XHF), a cyclone inlet 1 (XLJ 1) and a separator (FLQ) which are connected in sequence, and is used for realizing a mechanical compression function of low-temperature water vapor;
-the liquid separator (CYQ) is used for removing liquid entrained in the vaporized water vapor in the separator (FLQ);
the compressor (YSJ) may be a water vapor compressor in the form of roots, screws, centrifugation, or the like;
-the circulation valve (XHF) is used to turn on or off the compressed steam flowing to the separator (FLQ);
the cyclone inlet 1 (XLJ 1) is used for cyclone gravity separation of gas and liquid;
the workflow of the compression part is specifically as follows:
firstly, heat exchange is carried out on high-temperature gaseous steam from a rotational flow inlet 1 (XLJ 1) and spray liquid from bottom to top, partial vaporization occurs, and finally the gaseous steam flows to a liquid remover (CYQ); secondly, removing liquid carried in the water vapor by a liquid remover (CYQ), flowing to the suction side of a compressor (YSJ), mixing with water spray, and compressing; finally, when the exhaust valve (PQF) is closed and the circulation valve (XHF) is opened, the vapor compressed by the compressor (YSJ) flows to the circulation valve (XHF) and flows to the separator (FLQ) again through the swirl inlet 1 (XLJ 1), thereby completing the whole compression cycle.
Preferably, as shown in fig. 1, the steam exhaust part comprises a compressor (YSJ), a steam exhaust valve (PQF), a one-way valve (DXF), a rotational flow inlet 2 (XLJ 2) and a steam supplementing tank (BQG) which are connected in sequence, and is used for realizing the steam exhaust function of compressed steam;
the exhaust valve (PQF) is used for opening or closing the compressed steam flowing to the steam supplementing tank (BQG);
the check valve (DXF) is used for preventing the steam inside the steam supplementing tank (BQG) from flowing backwards;
the cyclone inlet 2 (XLJ 2) is used for cyclone gravity separation of gas and liquid;
the steam supplementing tank (BQG) is used for storing compressed steam from a compressor (YSJ) for use outside the system;
the working flow of the steam exhaust part is specifically as follows:
firstly, when the exhaust valve (PQF) is opened and the circulation valve (XHF) is closed, the steam compressed by the compressor (YSJ) flows to the exhaust valve (PQF) and then flows to the one-way valve (DXF); secondly, the air flows from the check valve (DXF) to the rotational flow inlet 2 (XLJ 2) again, and then flows to the steam supplementing tank (BQG); finally, the cyclone inlet 2 (XLJ 2) performs cyclone gravity separation on gas and liquid water, thereby completing the whole steam exhaust working cycle.
Preferably, as shown in fig. 1, the liquid return part comprises a vapor supplementing tank (BQG), a liquid return valve (HYF), a liquid return pump (HYB), a rotational flow inlet 1 (XLJ 1) and a separator (FLQ) which are connected in sequence, and is used for realizing the liquid return function of condensed water in the vapor supplementing tank (BQG);
the steam supplementing tank (BQG) is provided with a liquid level meter 2 (LWJ 2) for monitoring and adjusting the liquid level;
the liquid return valve (HYF) is used for adjusting the liquid return flow rate flowing to the separator (FLQ);
the liquid return pump (HYB) is used for sucking liquid return;
the working flow of the liquid return part is specifically as follows:
firstly, a liquid level meter 2 (LWJ 2) arranged on a steam supplementing tank (BQG) is used for monitoring and adjusting the liquid level, and condensed liquid water in the steam supplementing tank (BQG) flows to a liquid return valve (HYF); secondly, a liquid return valve (HYF) is opened, a liquid return pump (HYB) is started, and condensed liquid water flows to a rotational flow inlet 1 (XLJ 1); finally, the liquid enters the separator (FLQ) through the cyclone inlet 1 (XLJ 1), thereby completing the whole liquid return working cycle.
Preferably, as shown in fig. 1, the steam supply part comprises a steam supplementing tank (BQG) and a steam valve (ZQF) which are connected in sequence, and the steam supplementing tank is used for realizing the steam supply function outside the system;
the steam valve (ZQF) is used for regulating the flow rate of the water steam flowing to the outside of the system;
the working flow of the steam supply part is specifically as follows:
firstly, high-temperature gaseous steam from a rotational flow inlet 2 (XLJ 2) after rotational flow gravity separation flows to the top of a steam supplementing tank (BQG) from bottom to top; secondly, flowing from the steam supplementing tank (BQG) to a steam valve (ZQF) for regulating the flow of the water steam to the outside of the system; finally, the steam flows to the outside of the system through a steam valve (ZQF) for use, thereby completing the whole steam supply working cycle.
The technical problems, technical solutions and advantageous effects solved by the present invention have been further described in detail in the above-described embodiments, and it should be understood that the above-described embodiments are only illustrative of the present invention and are not intended to limit the present invention, and any modifications, equivalent substitutions, improvements, etc. within the spirit and principle of the present invention should be included in the scope of protection of the present invention.
Claims (8)
1. The mechanical compression type steam generation system is characterized by mainly comprising parts of water supplementing, spraying, water spraying, compression, steam discharging, liquid returning, steam supplying and the like; the water replenishing, spraying, water spraying, compressing and liquid returning parts are connected with each other and are crossed with the separator (FLQ); the water spray and compression section are connected and intersect a compressor (YSJ); the compression and exhaust sections are connected and intersect with an exhaust valve (PQF); the compression part and the liquid return part are connected and are intersected with the rotational flow inlet 1 (XLJ 1); the steam exhaust, liquid return and steam supply parts are mutually connected and are intersected with the steam supplementing tank (BQG).
2. The mechanically compressed steam generating system according to claim 1, wherein the water replenishing section comprises a water replenishing source (BSY), a water replenishing pump (BSB), a water replenishing valve (BSF), and a separator (FLQ) connected in this order.
3. A mechanically compressed steam generating system according to claim 2, characterized in that the spray section comprises a separator (FLQ), a spray Pump (PLB), a spray valve (PLF), a separator (FLQ) connected in sequence.
4. A mechanically compressed steam generating system according to claim 3, characterized in that the water spraying section comprises a separator (FLQ), a water spraying Pump (PSB), a water spraying valve (PSF), a compressor (YSJ) connected in sequence.
5. A mechanically compressed steam generating system according to claim 4, characterized in that the compression section comprises a separator (FLQ), a liquid separator (CYQ), a compressor (YSJ), a circulation valve (XHF), a swirl inlet 1 (XLJ 1), a separator (FLQ) connected in sequence.
6. The mechanically compressed steam generating system according to claim 5, wherein the steam exhaust section comprises a compressor (YSJ), a steam exhaust valve (PQF), a check valve (DXF), a swirl inlet 2 (XLJ 2), a steam make-up tank (BQG) connected in this order.
7. The mechanically compressed steam generating system according to claim 6, wherein the liquid return part comprises a vapor supplementing tank (BQG), a liquid return valve (HYF), a liquid return pump (HYB), a cyclone inlet 1 (XLJ 1) and a separator (FLQ) which are connected in sequence.
8. The mechanically compressed steam generating system according to claim 7, wherein the steam supply part comprises a steam supplementing tank (BQG) and a steam valve (ZQF) connected in sequence.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202211726764.XA CN116045265A (en) | 2022-12-30 | 2022-12-30 | Mechanical compression type steam generation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202211726764.XA CN116045265A (en) | 2022-12-30 | 2022-12-30 | Mechanical compression type steam generation system |
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| Publication Number | Publication Date |
|---|---|
| CN116045265A true CN116045265A (en) | 2023-05-02 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202211726764.XA Pending CN116045265A (en) | 2022-12-30 | 2022-12-30 | Mechanical compression type steam generation system |
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| CN (1) | CN116045265A (en) |
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- 2022-12-30 CN CN202211726764.XA patent/CN116045265A/en active Pending
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