CN208504359U - A kind of Novel steam device utilizing residual heat of return water - Google Patents
A kind of Novel steam device utilizing residual heat of return water Download PDFInfo
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- CN208504359U CN208504359U CN201821020425.9U CN201821020425U CN208504359U CN 208504359 U CN208504359 U CN 208504359U CN 201821020425 U CN201821020425 U CN 201821020425U CN 208504359 U CN208504359 U CN 208504359U
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- heat
- water
- return water
- storage tank
- vertical storage
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Abstract
The utility model discloses a kind of Novel steam device utilizing residual heat of return water, applied to cottonseed processing technical field, including return water main line, heat-exchanger pump, return water main line is connected to vertical storage tank, horizontal tank is connected to by waist valve outlet pipeline in the waist of vertical storage tank, the top of vertical storage tank is sequentially connected drying equipment and spray column by gas phase pipeline, storage resin container is connected with by soft water pipeline at the top of spray column, spray tower bottom is connected at the top of horizontal tank by mixed water lines, the bottom of horizontal tank connects outlet pipe, water in outlet pipe is delivered to boiler by heat-exchanger pump.The utility model improves the utilization rate of steam, reduces steam cost and production cost, improves the emptying effectiveness of heat-exchanger pump, saved boiler oil consumption.
Description
Technical field
The utility model relates to a kind of Novel steam device utilizing residual heat of return water, are applied to cottonseed processing technical field.
Background technique
As the energy is more and more in short supply, energy-saving pendulum in top priority, existing cottonseed adds for each manufacturing enterprise
There is the process using steam in its workshop of work enterprise, the steam come out from boiler room enters workshop, steam for drying,
The high-temperature condensation water of entrainment Low Temperature Steam (lack of gas) can be discharged after the equipment uses such as feed liquid separation, these high-temperature condensation waters are often straight
It connected return pipe to be connected in the recovery tank of normal pressure state, then boiler room is fed directly to by heat-exchanger pump.But directly from workshop
The high-temperature condensation water one side water temperature over-high of the equipment discharges such as drying, feed liquid separation, is easily damaged the sealing structure of heat-exchanger pump, together
When recovery tank in a large amount of steam presence, reduce the transfer efficiency of heat-exchanger pump, there are Some Enterprises to pass through in recovery tank directly
Cold soft water is injected, the water temperature of high-temperature condensation water is reduced；The Low Temperature Steam (lack of gas) carried secretly in another aspect high-temperature condensation water can not
It is effectively used, is directly discharged into air by return water upper box part, not only causes to waste, improve the production of enterprise indirectly
Cost can also carry out steam to paripheral zone, impact to workshop around.
Utility model content
The utility model technical issues that need to address are to provide a kind of Novel steam device utilizing residual heat of return water, improve
The utilization rate of steam reduces steam cost and production cost, improves the emptying effectiveness of heat-exchanger pump, saved boiler oil and disappeared
Consumption.
In order to solve the above technical problems, the technical scheme adopted by the utility model is:
A kind of Novel steam device utilizing residual heat of return water, including return water main line, heat-exchanger pump, return water main line are connected to vertical
Formula storage tank is connected to horizontal tank by waist valve outlet pipeline in the waist of vertical storage tank, passes through gas phase at the top of vertical storage tank
Pipeline is sequentially connected drying equipment and spray column, and spray column top is connected with storage resin container, spray column bottom by soft water pipeline
Portion is connected at the top of horizontal tank by mixed water lines, and the bottom of horizontal tank connects outlet pipe, and heat-exchanger pump will be in outlet pipe
Water is delivered to boiler.
Technical solutions of the utility model further improvement lies in that: water in return water main line is entered vertical with tangential way
In storage tank.
Technical solutions of the utility model further improvement lies in that: heat exchange filler is housed in the spray column.
Technical solutions of the utility model further improvement lies in that: the heat exchange filler be stainless steel ring.
By adopting the above-described technical solution, the technological progress that the utility model obtains is:
A kind of Novel steam device utilizing residual heat of return water of the utility model improves the utilization rate of steam, reduces steam
Cost and production cost improve the emptying effectiveness of heat-exchanger pump, have saved boiler oil consumption.
The utility model is by setting vertical storage tank, the folder that the equipment such as workshop drying, feed liquid separation can be made to come out
High-temperature condensation water with lack of gas is entered by return water main line carries out gas-liquid separation in vertical storage tank, lack of gas are separated, into
Enter and material is dried in an individual drying equipment, the first time for completing waste heat utilizes, and the high temperature separated is cold
When condensate enters horizontal tank from the waist valve outlet pipeline at the middle part of vertical storage tank, since lack of gas are separated, entrance is horizontal
Steam will not be entrained in the high-temperature condensation water of storage tank, the water temperature into horizontal tank also can decrease.
Lack of gas enter spray column after coming out in drying equipment, and the cold soft water of the brand-new to come from resin container enters spray
Top of tower is drenched, lack of gas and cold the soft water mixed heat transfer in spray column make lack of gas become water completely, do not have when flowing into horizontal tank
With the presence of gas, while realizing second of effective use of steam waste heat, the condensation of horizontal tank high temperature can also be reduced
The temperature of water makes there is no gas, to be conducive to improve the working efficiency that heat-exchanger pump pumps, the utility model in horizontal tank in this way
Structure compared with being directly added into cold soft water and reducing the temperature of high-temperature condensation water, except lack of gas discharge system, obtain lack of gas
It is recycled to abundant, the cold soft water dosage as supplement is also fewer, does not also have as to the horizontal tank of boiler conveying cold water
With the presence of gas, the emptying effectiveness of heat-exchanger pump is improved, has saved boiler oil consumption.
High-temperature condensation water in return water main line is entered in vertical storage tank with tangential way, due to pressure in return water main line
Effect be uniformly distributed so that high-temperature condensation water rotates on the inner wall of vertical storage tank, rotary force effect under steam rise,
Liquid sinks can be such that gas-liquid is effectively separated, and stainless steel ring heat exchange filler is arranged in spray column, can make lack of gas and cold soft water
Sufficiently heat exchange.
Detailed description of the invention
Fig. 1 is the utility model structure diagram；
Wherein, 1, return water main line, 2, vertical storage tank, 3, gas phase pipeline, 4, drying equipment, 5, spray column, 6, resin container,
7, soft water pipeline, 8, waist valve outlet pipeline, 9, horizontal tank, 10, mixed water lines, 11, heat-exchanger pump, 12, outlet pipe.
Specific embodiment
The utility model is described in further details below with reference to embodiment:
Such as Fig. 1, a kind of Novel steam device utilizing residual heat of return water, including return water main line 1, heat-exchanger pump 11, return water supervisor
Road 1 is connected to vertical storage tank 2, is connected to horizontal tank 9, vertical storage tank by waist valve outlet pipeline 8 in the waist of vertical storage tank 2
2 top is sequentially connected drying equipment 4 and spray column 5 by gas phase pipeline 3, is connected at the top of spray column 5 by soft water pipeline 7
Resin container 6 is stored, 5 bottom of spray column is connected to 9 top of horizontal tank, the bottom connection of horizontal tank 9 by mixed water lines 10
Water in outlet pipe 12 is delivered to boiler by outlet pipe 12, heat-exchanger pump 11.By the way that vertical storage tank 2 is arranged, workshop can be made
The high-temperature condensation water for the entrainment lack of gas that the equipment such as drying, feed liquid separation come out by return water main line 1 into vertical storage tank 2 into
Row gas-liquid separation, lack of gas are separated, and into drying in an individual drying equipment 4 to material, complete waste heat
It utilizes for the first time, and the high-temperature condensation water separated enters horizontal tank from the waist valve outlet pipeline 8 at the middle part of vertical storage tank 2
When 9, since lack of gas are separated, into steam will not be entrained in the high-temperature condensation water of horizontal tank 9, into horizontal tank
9 water temperature also can decrease.Lack of gas enter spray column 5 after coming out in drying equipment 4, and it is new to come from resin container 6
The cold soft water of system enters 5 top of spray column, and lack of gas and cold the soft water mixed heat transfer in spray column 5 make lack of gas become water completely,
There is no gas presence when flowing into horizontal tank 9, while realizing second of effective use of steam waste heat, can also reduce
The temperature of 9 high temperature condensed water of horizontal tank makes to be conducive to improve the pump of heat-exchanger pump 11 in this way there is no gas in horizontal tank 9
The working efficiency of water, the structure of the utility model be not weary compared with being directly added into cold soft water and reducing the temperature of high-temperature condensation water
Except gas discharge system, lack of gas is made to be fully recycled, the cold soft water dosage as supplement is also fewer, as to boiler
The horizontal tank 9 for conveying cold water also exists without gas, improves the emptying effectiveness of heat-exchanger pump 11, has saved boiler oil and disappeared
Consumption.
Perpendicular to the axis of vertical storage tank 2, the water in return water main line 1 is entered vertical return water main line 1 with tangential way
In storage tank 2, due to the effect of pressure in return water main line, uniformly divide so that high-temperature condensation water rotates on the inner wall of vertical storage tank
Cloth, the steam rising under rotary force effect, liquid sinks, can be such that gas-liquid is effectively separated；Equipped with heat exchange in spray column 5
Filler, heat exchange filler are stainless steel ring, and setting stainless steel ring heat exchange filler, can make lack of gas and cold soft water abundant in spray column 5
Heat exchange.
When utility model works, the high temperature of the entrainment lack of gas come out from equipment such as workshop drying, feed liquid separation is cold
Condensate is entered in vertical storage tank 2 by return water main line 1 carries out gas-liquid separation, and the high-temperature condensation water separated is from vertical storage tank
The waist valve outlet pipeline 8 at 2 middle part enters horizontal tank 5, gas phase pipeline of the lack of gas being separated from 2 top of vertical storage tank
It is flowed out in 3, into drying in an individual drying equipment 4 to material, the first time for completing waste heat is utilized, and lack of gas are from baking
Enter spray column 5 after coming out in dry equipment 4, the cold soft water of the brand-new to come from resin container 6 enters spray by soft water pipeline 7
5 top of tower, lack of gas and cold the soft water mixed heat transfer in spray column 5, while realizing second of effective use of steam waste heat,
The soft water that finishes of exchanging heat is flowed into horizontal tank 9 by mixed water lines 10, the structure of the utility model and is directly added into cold soft water
The temperature for reducing high-temperature condensation water is compared, and except lack of gas discharge system, lack of gas is made to be fully recycled, as supplement
Cold soft water dosage it is also fewer, as to boiler conveying cold water horizontal tank 9 also without gas exist, improve heat-exchanger pump
11 emptying effectiveness, has saved boiler oil consumption, and mixed high-temperature condensation water enters water outlet from the bottom of horizontal tank 9
Water in outlet pipe 12 is delivered to boiler by pipe 12, heat-exchanger pump 11.
A kind of Novel steam device utilizing residual heat of return water of the utility model improves the utilization rate of steam, reduces steam
Cost and production cost improve the emptying effectiveness of heat-exchanger pump, have saved boiler oil consumption.
Claims (4)
1. a kind of Novel steam device utilizing residual heat of return water, including return water main line (1), heat-exchanger pump (11), it is characterised in that: return
Water main line (1) is connected to vertical storage tank (2), vertical storage tank (2) waist by waist valve outlet pipeline (8) be connected to it is horizontal
The top of storage tank (9), vertical storage tank (2) is sequentially connected drying equipment (4) and spray column (5), spray column by gas phase pipeline (3)
(5) top is connected with storage resin container (6) by soft water pipeline (7), and spray column (5) bottom is connected to by mixed water lines (10)
At the top of horizontal tank (9), the bottom of horizontal tank (9) connects outlet pipe (12), and heat-exchanger pump (11) is by the water in outlet pipe (12)
It is delivered to boiler.
2. a kind of Novel steam device utilizing residual heat of return water according to claim 1, it is characterised in that: return water main line
(1) water in is entered in vertical storage tank (2) with tangential way.
3. a kind of Novel steam device utilizing residual heat of return water according to claim 1, it is characterised in that: the spray column
(5) equipped with heat exchange filler in.
4. a kind of Novel steam device utilizing residual heat of return water according to claim 3, it is characterised in that: the heat exchange filler
For stainless steel ring.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821020425.9U CN208504359U (en) | 2018-06-29 | 2018-06-29 | A kind of Novel steam device utilizing residual heat of return water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821020425.9U CN208504359U (en) | 2018-06-29 | 2018-06-29 | A kind of Novel steam device utilizing residual heat of return water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208504359U true CN208504359U (en) | 2019-02-15 |
Family
ID=65282002
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821020425.9U Active CN208504359U (en) | 2018-06-29 | 2018-06-29 | A kind of Novel steam device utilizing residual heat of return water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208504359U (en) |
-
2018
- 2018-06-29 CN CN201821020425.9U patent/CN208504359U/en active Active
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