CN212457071U - Long-distance steam pipe network pressure loss control system in resident heating field - Google Patents

Abstract

The utility model discloses a control system of long defeated steam pipe network pressure loss in resident heating field sets up the heat supply initial station at steam pipe network terminal, retrieves long defeated steam condensate that supplies to power plant through the female pipe of condensate return. The long-distance steam transmission pipe network is divided into a plurality of pipe sections, pressure and temperature measuring points are arranged at high density, and the specific volume of steam at each position along the line is monitored in real time. The condensed water return pipelines are arranged in parallel along the long-distance steam pipe network, the pressure is increased by a booster pump in a heat supply initial station, the condensed water is sprayed into each steam pipe section, and the water spraying amount is subjected to post-feedback regulation by the specific volume of the steam after the water spraying point. The flow rate of the steam is controlled to be constant at an initial value based on high density monitoring and water spraying temperature reduction, and then the pressure loss along the whole steam pipe network is controlled within a design range.

Description

Long-distance steam pipe network pressure loss control system in resident heating field

[ technical field ] A method for producing a semiconductor device

The utility model relates to a control system of long distance steam pipe network pressure loss in resident's heating field.

[ background of the invention ]

With the social development and the continuous adjustment of energy industry structures and the continuous adjustment of power utilization structures, the coal-fired power generating set gradually changes from a traditional power supply main body to a comprehensive energy service base to supply electric power, heat, long-distance industrial steam, high-pressure industrial air, fresh water and the like to the outside. With the rapid development of heat preservation technology, the radiation radius of externally conveyed industrial steam is continuously increased by the coal-fired generator set through heat supply transformation, clean coal-fired centralized heat supply is promoted to replace dispersed coal-fired fuel boiler rooms with heavy pollution and high energy consumption, effective reduction and control of regional atmospheric pollutant emission are facilitated, and the profitability and sustainable development capability of the coal-fired generator set are facilitated to be improved.

The resident heating field has two technical routes of long-distance hot water transmission and long-distance steam transmission. The main contents of the long-distance hot water delivery scheme are as follows: a heat supply initial station is arranged in a coal-fired power generating unit plant, steam is extracted from a certain position of a thermodynamic system to a surface type heat supply network heater and heat supply circulating water for heat exchange, condensed water is recovered to a condenser or a deaerator, the heat supply circulating water is conveyed to a town heat supply network through a long-distance hot water pipe network, and cold water after heat exchange flows back to the heat supply initial station in the power plant to form a cycle. The long-distance steam transmission scheme mainly comprises the following contents: a heat supply initial station is arranged near a town, steam is extracted from a certain position of steam-water circulation of a coal-fired power generating unit and is conveyed to the heat supply initial station through a long-distance steam conveying pipe network, heat exchange is carried out between a surface type heat supply network heater and heat supply circulating water, and drain water after steam condensation is pressurized through a booster pump and then is recycled to a unit thermodynamic system in a return water main pipe.

The scheme of the long-distance steam supply pipe network in the residential heating field is basically similar to that of the long-distance steam supply pipe network in the industrial production field, and the main difference is that the condensed water is recovered in the former and the condensed water is not recovered due to factors such as production process and the like. The thermal indexes of the long-distance industrial steam pipeline network include pipeline temperature drop, pipeline pressure drop, steam pipeline network loss rate and the like.

Cooling the pipeline:

in the formula: delta t is the temperature drop of the pipeline, DEG C/km; t is t₁,t₂Respectively the starting point temperature and the end point temperature of the steam pipe network, DEG C; l is the steam pipe length, km.

Pressure drop of the pipeline:

in the formula: delta P is the temperature drop of the pipeline, MPa/km; p₁,P₂Respectively the starting point pressure and the end point pressure of the steam pipe network, namely MPa;

loss rate of steam pipe network

In the formula: g is the mass loss rate of the steam pipe network and is a dimensionless number; q is the heat loss rate of the steam pipe network and is a dimensionless number; g₁,G₂Respectively the starting point mass flow and the end point mass flow of the steam pipe network, t/h; h is₁,h₂Respectively is the starting point steam enthalpy value and the terminal point steam enthalpy value of the steam pipe network, kJ/kg.

The temperature drop of the pipeline depends on the heat insulation material and performance of the pipeline.

The pipe pressure drop is proportional to the internal steam flow rate.

The through-flow diameter of the pipe network is increased, the flow rate of steam is low, the pressure drop of the steam pipe network is reduced, the operation cost is further reduced, and the construction investment of the pipe network is increased in reverse. Therefore, the reasonable pipeline temperature drop coefficient and pressure drop coefficient can effectively balance the dynamic contradiction relationship between the operation cost and the construction investment of the steam pipe network project

The specific volume of the water vapor is in inverse proportion to the vapor pressure and in proportion to the vapor temperature: the lower the vapor pressure, the higher the specific volume; the higher the steam temperature, the lower the specific volume. At present, the steam pipe network project set by the pipeline specification is applied in a large scale due to the high-performance heat-insulating material, the pipeline flows along with steam, the steam starting point is used as a comparison reference, the steam specific volume is increased due to pressure drop and temperature drop along with the flow of the steam, the steam flow speed is increased, the pressure drop is increased, meanwhile, the temperature drop is basically maintained unchanged, the steam flow speed in the whole pipe network system is faster and faster, the steam pressure drop is larger, and the economical efficiency and the laying radius of a long-distance pipe network are affected.

[ Utility model ] content

An object of the utility model is to solve the problem among the prior art, provide a control system of long defeated steam pipe network pressure loss in resident heating field, the pressure loss of effective control long defeated steam pipe network is based on high density monitoring and water spray desuperheating and is invariable with the control steam velocity of flow, and then controls the system and the method of whole steam pipe network pressure loss along the line.

In order to achieve the above purpose, the utility model adopts the following technical scheme to realize:

the utility model provides a control system that long distance steam pipe network pressure loss in resident's heating field, includes:

the long-distance steam pipeline comprises a plurality of steam pipe sections, and each steam pipe section is provided with a steam pressure measuring point and a steam temperature measuring point;

the condensation water pipe network comprises a condensation water main pipe, a condensation water ring pipe and a plurality of paths of condensation water branch pipes, and the condensation water ring pipe is sleeved on the long-distance steam transmission pipeline; each path of condensed water branch pipe is respectively connected to a corresponding pipe section on the long-distance steam pipeline, a condensed water flow measuring point and a condensed water spraying valve group are arranged on each path of condensed water branch pipe, the opening degree of the condensed water spraying valve group is adjusted by taking the specific volume of the steam after the water spraying point as the guide, and the specific volume of the steam is determined by calculating the steam pressure, the temperature and the flow at the position;

the heat supply first station is connected to a steam conveying end point of the long-distance steam conveying pipeline, surface heat exchange is carried out between the surface heat exchanger and circulating water of a heat supply network, condensed water is pressurized by the booster pump and then is parallel to the long-distance steam conveying pipeline network, and the condensed water is recycled to the coal-fired power plant through the condensate water return main pipe, so that the quality balance of steam and water is realized.

The utility model discloses further improvement lies in:

the condensation water ring pipe is provided with a plurality of atomizing nozzles, the condensation water ring pipe is communicated with the condensation water main pipe through a condensation water branch, and the condensation water ring pipe is communicated with the long-distance steam conveying pipeline through the atomizing nozzles.

At least 5 atomizing nozzles are uniformly arranged on the condensation water ring pipe on the outer side of each steam pipe section in the circumferential direction on the long-distance steam transmission pipeline.

Compared with the prior art, the utility model discloses following beneficial effect has:

the utility model divides the long-distance steam pipe network into a plurality of pipe sections, each pipe section is provided with a steam pressure measuring point, a temperature measuring point and a flow measuring point, parameters such as steam flow, pressure and temperature are transmitted to a control platform, and the steam flow velocity of each pipe section is monitored in real time; set up condensate system along long defeated steam pipe network, through the condensate flow of adjusting each steam pipe network section, reasonable control steam temperature and steam velocity of flow, and then effective control long defeated steam pipe network steam pressure loss is in the design interval, is favorable to widening steam transport length.

[ description of the drawings ]

In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings that are required to be used in the embodiments will be briefly described below, it should be understood that the following drawings only illustrate some embodiments of the present invention, and therefore should not be considered as limiting the scope, and for those skilled in the art, other related drawings can be obtained according to the drawings without inventive efforts.

FIG. 1 is a schematic view of the system for effectively controlling pressure loss of a long-distance steam pipe network according to the present invention;

fig. 2 is a schematic structural view of the condensed water ring pipe and the long-distance steam pipeline of the present invention.

Wherein: 1-long steam transmission pipeline; 2-condensation water main pipe; 3-measuring point of condensate flow; 4-steam pressure measuring point; 5-measuring the steam temperature; 6-a condensed water ring pipe; 7-atomizing nozzle.

[ detailed description ] embodiments

In order to make the objects, technical solutions and advantages of the embodiments of the present invention clearer, the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are some, but not all, embodiments of the present invention. The components of embodiments of the present invention, as generally described and illustrated in the figures herein, may be arranged and designed in a wide variety of different configurations.

Thus, the following detailed description of the embodiments of the present invention, presented in the accompanying drawings, is not intended to limit the scope of the invention, as claimed, but is merely representative of selected embodiments of the invention. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative efforts belong to the protection scope of the present invention.

It should be noted that: like reference numbers and letters refer to like items in the following figures, and thus, once an item is defined in one figure, it need not be further defined and explained in subsequent figures.

In the description of the embodiments of the present invention, it should be noted that, if the terms "upper", "lower", "horizontal", "inner", etc. indicate the orientation or position relationship based on the orientation or position relationship shown in the drawings, or the orientation or position relationship that the product of the present invention is usually placed when in use, the description is only for convenience of description and simplification, but the indication or suggestion that the device or element to be referred to must have a specific orientation, be constructed and operated in a specific orientation, and thus, should not be interpreted as limiting the present invention. Furthermore, the terms "first," "second," and the like are used merely to distinguish one description from another, and are not to be construed as indicating or implying relative importance.

Furthermore, the term "horizontal", if present, does not mean that the component is required to be absolutely horizontal, but may be slightly inclined. For example, "horizontal" merely means that the direction is more horizontal than "vertical" and does not mean that the structure must be perfectly horizontal, but may be slightly inclined.

In the description of the embodiments of the present invention, it should be further noted that unless explicitly stated or limited otherwise, the terms "disposed," "mounted," "connected," and "connected" should be interpreted broadly, and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood according to specific situations by those skilled in the art.

The present invention will be described in further detail with reference to the accompanying drawings:

referring to fig. 1 and 2, the long-distance steam transmission pipe network pressure loss control system in the residential heating field of the present invention comprises a long-distance steam transmission pipe 1 and a condensed water pipe network; the long-distance steam transmission pipeline 1 comprises a plurality of steam pipe sections, and each steam pipe section is provided with a steam pressure measuring point 4 and a steam temperature measuring point 5; at least 5 atomizing nozzles 7 are uniformly arranged on the periphery of the long steam transmission pipeline 1 and on the condensed water ring pipe 6 at the outer side of each steam pipe section. The condensed water pipe network comprises a condensed water main pipe 2, a condensed water ring pipe 6 and a plurality of paths of condensed water branch pipes, wherein the condensed water ring pipe 6 is sleeved on the long-distance steam transmission pipeline 1; each path of condensed water branch pipe is respectively connected to the corresponding pipe section on the long-distance steam pipeline 1, a condensed water flow measuring point 3 and a condensed water spraying valve group are arranged on each path of condensed water branch pipe, the opening degree of the condensed water spraying valve group is adjusted by taking the specific volume of the steam behind the water spraying point as the guide, and the specific volume of the steam is determined by the calculation of the steam pressure, the temperature and the flow at the position. The condensation water ring pipe 6 is provided with a plurality of atomizing nozzles 7, the condensation water ring pipe 6 is communicated with the condensation water main pipe 2 through a condensation water branch, and the condensation water ring pipe 6 is communicated with the long-distance steam pipeline 1 through the atomizing nozzles 7.

The utility model also discloses a control method of long distance steam pipe network pressure loss in resident heating heat supply field, including following step:

step 1, measuring the steam flow G of the initial end of the long-distance steam pipeline 1₀Pressure P₀And temperature T₀Calculating to obtain the initial stage steam flow velocity V₀；

Step 2, the pipe section of the long-distance steam pipeline 1 is counted by the starting end of the long-distance steam pipeline 1, the first section is the 1 st steam section, and the rest is the nth steam section; the 1 st steam section generates steam pressure drop, temperature drop and mass loss along with the flow and heat dissipation of steam, and the steam pressure P after a water spraying point is measured₁And temperature T₁And steam flow rate G₁Wherein G is₁＝G₀+G_1j，G_1jFor the flow of condensate, in V₀＝V₁Adjusting the flow of the condensate water of the 1 st steam section as a reference;

and step 3, taking the adjustment process of the steam section 1 as an example, sequentially adjusting the condensate flow of the rest steam sections to keep the steam flow rate of the whole long-distance steam pipeline 1 constant, and further controlling the pressure loss of the whole long-distance steam pipeline 1 along the line to be constant and to be a design value.

The utility model discloses a structural principle:

the whole long-distance steam pipeline 1 is artificially divided into a plurality of pipeline sections from the starting end of a long-distance steam supply pipeline network at a steam source of a coal-fired power plant to a terminal at a user demand side, steam pressure and temperature measuring points are arranged at high density, and measuring results are remotely transmitted to a heat supply pipe control center for data monitoring and operation adjustment.

A heating initial station is arranged at a steam pipe network terminal in the heating field, surface heat exchange is carried out between a surface heat exchanger and heat supply network circulating water, after steam is condensed and is pressurized by a booster pump, the condensed water is parallel to a steam pipe network and is recycled to a coal-fired power plant through a condensed water return main pipe, and the quality balance of steam and water is realized. And each pipe section of the condensed water return main pipe is provided with a valve group, condensed water is sprayed into each steam pipe section, and the water spraying amount is subjected to post feedback regulation by the specific volume of steam after a water spraying point. The opening of the water spray regulating valve is regulated by taking the specific volume of the steam after the water spray point as the guide, and the specific volume of the steam is determined by calculating the steam pressure, the temperature and the flow at the position. The condensate system is in the form of a loop pipe, and the atomizing nozzles 7 are uniformly arranged in the steam pipeline. The condensate system is pressurized inside the coal fired power plant by a booster pump.

The utility model discloses be provided with long-distance transport steam supply management and control platform, the adjustment benchmark keeps invariable for the steam flow velocity of whole steam pipe network along the line.

The steam flow, pressure and temperature measuring points G are arranged at the starting end of the long-distance steam transmission pipe network, namely the steam extraction part of the coal-fired power generating set₀、P₀And T₀Calculating to obtain the initial stage steam flow velocity V₀。

At the steam pipe section 1, steam pressure drop, temperature drop and mass loss occur as the steam flows and dissipates heat. The steam pressure and the temperature after the temperature reduction water spraying point are respectively P₁、T₁Steam flow of G₁Wherein G is₁＝G₀+G_1j，G_1jFor the flow of condensate, in V₀＝V₁Is based onAnd (6) adjusting the flow of the condensate water of the pipe network section.

By analogy, the flow rate of the condensed water of each steam pipe network is adjusted, so that the flow rate of the steam along the whole steam pipe network is kept constant, and the pressure loss of the whole steam pipe network along the line is controlled to be constant and is a design value.

The utility model has the advantages of it is following:

the utility model discloses the long and medium transport steam supply pipe network condensate retrieves. The long-distance steam transmission pipe network is divided into a plurality of pipe sections, pressure and temperature measuring points are arranged at high density, and the specific volume of steam at each position along the line is monitored in real time. Condensed water pipelines are arranged in parallel along the long-distance steam transmission pipe network, a booster pump is used for pressurizing in the power plant, condensed water is sprayed into each steam pipe section, and the water spraying amount is subjected to post-feedback regulation by the specific volume of steam after the water spraying point. The flow rate of the steam is controlled to be constant at an initial value based on high density monitoring and water spraying temperature reduction, and then the pressure loss along the whole steam pipe network is controlled within a design range. The utility model discloses based on high density steam temperature, pressure and flow monitoring and calculation, rationally spout into the condensate water, reasonable control steam temperature, and then effective control long-distance steam pipe net steam pressure loss is in the design interval, is favorable to widening steam transport length.

The above is only a preferred embodiment of the present invention, and is not intended to limit the present invention, and various modifications and changes will occur to those skilled in the art. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.

Claims (3)

1. The utility model provides a control system that long distance steam pipe network pressure loss in resident's heating field which characterized in that includes:

the long-distance steam pipeline (1) comprises a plurality of steam pipeline sections, and each steam pipeline section is provided with a steam pressure measuring point (4) and a steam temperature measuring point (5);

the condensation water pipe network comprises a condensation water main pipe (2), a condensation water ring pipe (6) and a plurality of paths of condensation water branch pipes, wherein the condensation water ring pipe (6) is sleeved on the long-distance steam transmission pipeline (1); each path of condensed water branch pipe is respectively connected to a corresponding pipe section on the long-distance steam pipeline (1), a condensed water flow measuring point (3) and a condensed water spraying valve group are arranged on each path of condensed water branch pipe, the opening degree of the condensed water spraying valve group is adjusted by taking the specific volume of steam after the water spraying point as the guide, and the specific volume of the steam is determined by the steam pressure, the temperature and the flow calculation of the position;

the heat supply first station is connected to a steam conveying end point of the long-distance steam conveying pipeline (1), surface heat exchange is carried out between the surface heat exchanger and circulating water of a heat supply network, condensed water is pressurized by a booster pump and then is parallel to the long-distance steam conveying pipeline network, and the condensed water is recycled to the coal-fired power plant through a condensate water return main pipe, so that the quality balance of steam and water is realized.

2. The system for controlling the pressure loss of the long-distance steam pipe network in the resident heating field according to claim 1, wherein a plurality of atomizing nozzles (7) are arranged on the condensed water ring pipe (6), the condensed water ring pipe (6) is communicated with the condensed water main pipe (2) through a condensed water branch, and the condensed water ring pipe (6) is communicated with the long-distance steam pipe (1) through the atomizing nozzles (7).

3. The system for controlling the pressure loss of the long-distance steam transmission pipe network in the residential heating field according to claim 2, wherein at least 5 atomizing nozzles (7) are uniformly arranged on the long-distance steam transmission pipeline (1) in the circumferential direction on the condensed water annular pipe (6) at the outer side of each steam pipe section.

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