CN104180161A - Automatic steam saturation degree adjusting device - Google Patents
Automatic steam saturation degree adjusting device Download PDFInfo
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- CN104180161A CN104180161A CN201410404829.8A CN201410404829A CN104180161A CN 104180161 A CN104180161 A CN 104180161A CN 201410404829 A CN201410404829 A CN 201410404829A CN 104180161 A CN104180161 A CN 104180161A
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Abstract
The invention belongs to the field of pharmaceutical and food processing equipment and discloses an automatic steam saturation degree adjusting device which comprises a steam input pipeline (1) and a steam output pipeline (12). The automatic steam saturation degree adjusting device is characterized in that a steam input isolating valve (2) and an input temperature pressure monitor (3) are sequentially mounted on the steam input pipeline (1), a steam output stop valve (10) and an output temperature pressure monitor (11) are mounted on the steam output pipeline (12), a saturated steam passage, an unsaturated steam passage, a slightly-overheated steam passage and an excessively-overheated steam passage are connected on a pipeline between the input temperature pressure monitor (3) and the steam output pipeline (12) respectively, and the input temperature pressure monitor (3) is connected with and controls control valves in the saturated steam passage, the unsaturated steam passage, the slightly-overheated steam passage and the excessively-overheated steam passage through a cable conductor respectively to realize switching among the passages. The automatic steam saturation degree adjusting device can automatic judge steam saturation degree and perform automatic adjustment according to needs.
Description
Technical field
Vapo(u)rous degree automatic control tegulatingdevice, belongs to pharmacy and food processing plant field.
Background technique
Pharmaceutical equipment development is at present maked rapid progress, and various pharmaceutical equipments emerge in an endless stream.Thereby, utilization for steam is also more and more extensive, but the steam pipework mounting type of different pharmaceutical equipments etc. there are differences, so finally inputting the saturation ratio of the steam of pharmaceutical equipment also there are differences, such as the equipment having can be inputted saturated vapour, some equipment can be inputted unsaturated steam, and some equipment can be inputted superheated vapor.Because the steam of all devices all needs saturated vapour, so the steam supply under prior art cannot meet the demand of all devices.
Summary of the invention
The technical problem to be solved in the present invention is: overcome the deficiencies in the prior art, provide a kind of can automatic decision vapo(u)rous degree regulating as required, simple in structure and can conveniently be integrated into the vapo(u)rous degree automatic control tegulatingdevice in equipment.
The technical solution adopted for the present invention to solve the technical problems is: this vapo(u)rous degree automatic control tegulatingdevice, comprise steam input pipe and steam output pipe road, steam input isolating valve and input temperature-voltage monitor are installed on described steam input pipe successively, steam output stop valve and output temperature-voltage monitor are installed on steam output pipe road, between input temperature-voltage monitor and steam output pipe road, on pipeline, be connected with respectively saturated vapour passage, unsaturated steam passage, micro-superheated vapor passage and surpass hot vapour passage, input temperature-voltage monitor connects respectively by cable conductor and controls saturated vapour passage, unsaturated steam passage, micro-superheated vapor passage and the control valve surpassing in hot vapour passage are realized the switch operating between each passage.Input temperature-voltage monitor can be monitored the vapor pressure that enters steam input pipe, and control valve realization switching, by valve opening and closing, realizes the switch operating between each passage.
Further, described output temperature-voltage monitor connects steam output stop valve by cable conductor.
Described saturated vapour passage comprises steam input stop valve, steam input bypass valve and saturated vapour pipeline, saturated vapour pipeline is communicated with steam input pipe and steam output pipe road, steam input bypass valve is installed in saturated vapour pipeline, the anterior steam input stop valve of installing of steam input bypass valve, steam input stop valve connects input temperature-voltage monitor by cable conductor.Input temperature-voltage monitor is controlled the switching of steam input stop valve, if input temperature-voltage monitor judgement input steam is saturated vapour, input temperature-voltage monitor by cable conductor controls steam input stop valve, steam is inputted bypass valve and is opened, make steam enter saturated vapour pipeline, output temperature-voltage monitor is controlled steam output stop valve by cable conductor and is opened, directly output saturation steam.
Described unsaturated steam passage comprises unsaturated steam steam inlet valve, unsaturated steam pipeline, heating temperature-voltage monitor, heating equipment and steam intensification steam inlet valve, unsaturated steam pipeline connection steam input pipe and steam output pipe road, unsaturated steam steam inlet valve, heating equipment, heating temperature-voltage monitor and steam intensification steam inlet valve are installed in unsaturated steam pipeline, unsaturated steam steam inlet valve connects input temperature-voltage monitor by cable conductor, and heating temperature-voltage monitor connects respectively heating equipment and steam intensification steam inlet valve by cable conductor.If input temperature-voltage monitor judgement input steam is unsaturated steam, input temperature-voltage monitor is controlled unsaturated steam steam inlet valve by cable conductor and is opened, make steam enter unsaturated steam pipeline, heating temperature-voltage monitor is according to the unsaturation degree of steam, by cable conductor, controlling heating equipment heats steam, then control steam intensification steam inlet valve and open, output temperature-voltage monitor is controlled steam output stop valve by cable conductor and is opened, output saturation steam.
Preferably, described heating equipment is arranged between unsaturated steam steam inlet valve and heating temperature-voltage monitor.
Described micro-superheated vapor passage comprises admission buffer, buffering temperature-voltage monitor and steam buffer delivery valve, admission buffer is arranged between steam input pipe and steam output pipe road, buffering temperature-voltage monitor and drip pipe are installed on admission buffer, admission buffer rear portion connects steam buffer delivery valve, and buffering temperature-voltage monitor connects steam buffer delivery valve by cable conductor.
Further, described drip pipe is arranged on admission buffer bottom, and condensed water elimination valve is installed in drip pipe.Condensed water elimination valve connects buffering temperature-voltage monitor by cable conductor.If input temperature-voltage monitor judgement input steam is micro-superheated vapor, input temperature-voltage monitor is controlled steam input stop valve by cable conductor and is opened, make steam enter admission buffer, buffering temperature-voltage monitor judgement superheated vapor is cooled to be controlled steam buffer delivery valve by cable conductor after saturated vapour and opens, if cooling too much, buffering temperature-voltage monitor is controlled condensed water elimination valve by cable conductor and is opened, the unnecessary condensed water of draining, output temperature-voltage monitor is controlled steam output stop valve by cable conductor and is opened, output saturation steam.
Further, described steam buffer delivery valve is arranged between admission buffer and output temperature-voltage monitor.
The described hot vapour passage that surpasses comprises superheated vapor suction valve, superheated vapor pipeline, cooling unit, cooling temperature-voltage monitor, cooling steam inlet valve and admission buffer, superheated vapor pipeline one end connects steam input pipe, the other end connects cooling unit, cooling temperature-voltage monitor is installed on cooling unit, cooling unit connects admission buffer, and cooling steam inlet valve is installed between cooling unit and admission buffer.If input temperature-voltage monitor judgement input steam is for surpassing hot steam, input temperature-voltage monitor is controlled superheated vapor inlet open by cable conductor, steam is entered after superheated vapor pipeline by cooling unit surpassing the hot steam processing of lowering the temperature, its temperature drop degree is controlled by cooling temperature-voltage monitor, then cooling temperature-voltage monitor is controlled cooling steam inlet valve by cable conductor and is opened the steam make after cooling and enter admission buffer and carry out reducing temperature twice, or directly enter steam output pipe road, then by output temperature-voltage monitor, by cable conductor, controlling steam output stop valve opens, output saturation steam.
Further, described cooling temperature-voltage monitor connects cooling unit by cable conductor.
Compared with prior art, the beneficial effect that the technique scheme of this vapo(u)rous degree automatic control tegulatingdevice has is:
1, can also regulate as required by automatic decision vapo(u)rous degree: by input temperature-voltage monitor and saturated vapour passage, unsaturated steam passage, micro-superheated vapor passage being set and surpassing hot vapour passage, by steam in steam input pipe is carried out to intelligent decision, can be respectively unsaturated steam or superheated vapor be adjusted to saturated vapour and export, thereby meet the demand of all devices to saturated vapour.
2, simple in structure and can conveniently be integrated into equipment: this vapo(u)rous degree automatic control tegulatingdevice just can be realized automatic decision and adjusting by temperature-voltage monitor and pipeline and valve are set, simple in structure, integrated installation is in equipment, economic and practical easily, has larger promotional value.
Accompanying drawing explanation
Fig. 1 is this vapo(u)rous degree automatic control tegulatingdevice structural representation.
Wherein: 1, steam input pipe 2, steam input isolating valve 3, input temperature-voltage monitor 4, superheated vapor suction valve 5, steam input stop valve 6, steam input bypass valve 7, admission buffer 8, buffering temperature-voltage monitor 9, steam buffer delivery valve 10, steam output stop valve 11, output temperature-voltage monitor 12, steam output pipe road 13, cooling unit 14, cooling temperature-voltage monitor 15, cooling steam inlet valve 16, unsaturated steam steam inlet valve 17, heating equipment 18, heating temperature-voltage monitor 19, intensification steam inlet valve 20, condensed water elimination valve 100, saturated vapour pipeline 101, unsaturated steam pipeline 102, superheated vapor pipeline.
Embodiment
Fig. 1 is the most preferred embodiment of this vapo(u)rous degree automatic control tegulatingdevice, and below in conjunction with accompanying drawing 1, the present invention will be further described.
With reference to accompanying drawing 1: vapo(u)rous degree automatic control tegulatingdevice, comprises steam input pipe 1 and steam output pipe road 12.Steam input isolating valve 2 and input temperature-voltage monitor 3 are installed on steam input pipe 1 successively, steam output stop valve 10 and output temperature-voltage monitor 11 are installed on steam output pipe road 12, and output temperature-voltage monitor 11 connects steam output stop valve 10 by cable conductor.Between input temperature-voltage monitor 3 and steam output pipe road 12, on pipeline, be connected with respectively saturated vapour passage, unsaturated steam passage, micro-superheated vapor passage and surpass hot vapour passage, input temperature-voltage monitor 3 connects respectively by cable conductor and controls saturated vapour passage, unsaturated steam passage, micro-superheated vapor passage and realize the switch operating between each passage over the control valve in hot vapour passage.
Saturated vapour passage comprises steam input stop valve 5, steam input bypass valve 6 and saturated vapour pipeline 100, saturated vapour pipeline 100 is communicated with steam input pipe 1 and steam output pipe road 12, steam input bypass valve 6 is installed in saturated vapour pipeline 100, the anterior steam input stop valve 5 of installing of steam input bypass valve 6, steam input stop valve 5 connects input temperature-voltage monitor 3 by cable conductor.
Unsaturated steam passage comprises unsaturated steam steam inlet valve 16, unsaturated steam pipeline 101, heating temperature-voltage monitor 18, heating equipment 17 and steam intensification steam inlet valve 19, unsaturated steam pipeline 101 is communicated with steam input pipe 1 and steam output pipe road 12, unsaturated steam steam inlet valve 16 is installed in unsaturated steam pipeline 101 successively, heating equipment 17, heating temperature-voltage monitor 18 and steam intensification steam inlet valve 19, unsaturated steam steam inlet valve 16 connects input temperature-voltage monitor 3 by cable conductor, heating temperature-voltage monitor 18 connects respectively heating equipment 17 and steam intensification steam inlet valve 19 by cable conductor.
Micro-superheated vapor passage comprises admission buffer 7, buffering temperature-voltage monitor 8 and steam buffer delivery valve 9, admission buffer 7 is arranged between steam input pipe 1 and steam output pipe road 12, buffering temperature-voltage monitor 8 and condensed water elimination valve 20 are installed on admission buffer 7, admission buffer 7 rear portions connect steam buffer delivery valve 9, and buffering temperature-voltage monitor 8 connects steam buffer delivery valve 9 and condensed water elimination valve 20 by cable conductor.
Surpass hot vapour passage and comprise superheated vapor suction valve 4, superheated vapor pipeline 102, cooling unit 13, cooling temperature-voltage monitor 14, cooling steam inlet valve 15 and admission buffer 7, superheated vapor pipeline 102 one end connect steam input pipe 1, the other end connects cooling unit 13, cooling temperature-voltage monitor 14 is installed on cooling unit 13, cooling unit 13 connects admission buffer 7 and steam output pipe road 12 simultaneously, and cooling steam inlet valve 15 is installed between cooling unit 13 and admission buffer 7.Cooling temperature-voltage monitor 14 connects cooling unit 13 by cable conductor.
The steam that need to export 3 kilograms (absolute pressures) of take is example, and working principle and the process of this vapo(u)rous degree automatic control tegulatingdevice are as follows:
If input temperature-voltage monitor 3 judgement input steam are 3 kilograms of absolute pressures, the saturated vapour that temperature is 149 ℃, input temperature-voltage monitor 3 is controlled steam input stop valve 5,6 unlatchings of steam input bypass valve by cable conductor, make steam enter saturated vapour pipeline 100, output temperature-voltage monitor 11 is controlled steam output stop valve 10 by cable conductor and is opened, directly output saturation steam;
If input temperature-voltage monitor 3 judgement input steam are 3 kilograms of absolute pressures, the unsaturated steam that temperature is 139 ℃, input temperature-voltage monitor 3 is controlled unsaturated steam steam inlet valve 16 by cable conductor and is opened, make steam enter unsaturated steam pipeline 101, heating temperature-voltage monitor 18 is according to the unsaturation degree of steam, by cable conductor, control 17 pairs of heating equipments and be steam heated to 147.5 ℃, then controlling steam intensification steam inlet valve 19 opens, output temperature-voltage monitor 11 is controlled steam output stop valve 10 by cable conductor and is opened, 3 kilograms of output absolute pressures, the saturated vapour that temperature is 149 ℃,
If input temperature-voltage monitor 3 judgement input steam are 3 kilograms of absolute pressures, micro-superheated vapor that temperature is 152 ℃, input temperature-voltage monitor 3 is controlled steam input stop valve 5 by cable conductor and is opened, make steam enter admission buffer 7, after buffering temperature-voltage monitor 8 judgement superheated vapors are cooled to 149 ℃, by cable conductor, controlling steam buffer delivery valve 9 opens, if lowered the temperature, as many as was 148 ℃, buffering temperature-voltage monitor 8 is controlled condensed water elimination valve 20 by cable conductor and is opened, the unnecessary condensed water of draining, output temperature-voltage monitor 11 is controlled steam output stop valve 10 by cable conductor and is opened, 2.9 kilograms of output absolute pressures, the saturated vapour of temperature 147.5 ℃ (temperature-fall period is slightly lossy),
If input temperature-voltage monitor 3 judgement input steam are 3 kilograms of absolute pressures, 160 ℃ of temperature surpass hot steam, input temperature-voltage monitor 3 is controlled superheated vapor suction valve 4 by cable conductor and is opened, steam is entered after superheated vapor pipeline 102 by 13 pairs of cooling units and surpass the hot steam processing of lowering the temperature, its temperature drop degree is controlled by cooling temperature-voltage monitor 14, then cooling temperature-voltage monitor 14 is controlled cooling steam inlet valve 15 by cable conductor and is opened and make to be cooled to the steam of 150 ℃ and enter admission buffer 7 and carry out reducing temperature twice, or directly enter steam output pipe road 12, then by output temperature-voltage monitor 11, by cable conductor, controlling steam output stop valve 10 opens, 3 kilograms of output absolute pressures, the saturated vapour that temperature is 149 ℃.
The above, be only preferred embodiment of the present invention, is not the present invention to be done to the restriction of other form, and any those skilled in the art may utilize the technology contents of above-mentioned announcement to be changed or be modified as the equivalent embodiment of equivalent variations.But every technical solution of the present invention content that do not depart from, any simple modification, equivalent variations and the remodeling above embodiment done according to technical spirit of the present invention, still belong to the protection domain of technical solution of the present invention.
Claims (10)
1. vapo(u)rous degree automatic control tegulatingdevice, comprise steam input pipe (1) and steam output pipe road (12), it is characterized in that: steam input isolating valve (2) and input temperature-voltage monitor (3) are installed on described steam input pipe (1) successively, steam output stop valve (10) and output temperature-voltage monitor (11) are installed on steam output pipe road (12), between input temperature-voltage monitor (3) and steam output pipe road (12), on pipeline, be connected with respectively saturated vapour passage, unsaturated steam passage, micro-superheated vapor passage and surpass hot vapour passage, input temperature-voltage monitor (3) connects respectively by cable conductor and controls saturated vapour passage, unsaturated steam passage, micro-superheated vapor passage and the control valve surpassing in hot vapour passage are realized the switch operating between each passage.
2. vapo(u)rous degree automatic control tegulatingdevice according to claim 1, is characterized in that: described output temperature-voltage monitor (11) connects steam output stop valve (10) by cable conductor.
3. vapo(u)rous degree automatic control tegulatingdevice according to claim 1, it is characterized in that: described saturated vapour passage comprises steam input stop valve (5), steam input bypass valve (6) and saturated vapour pipeline (100), saturated vapour pipeline (100) is communicated with steam input pipe (1) and steam output pipe road (12), steam input bypass valve (6) is installed in saturated vapour pipeline (100), the anterior steam input stop valve (5) of installing of steam input bypass valve (6), steam input stop valve (5) connects input temperature-voltage monitor (3) by cable conductor.
4. vapo(u)rous degree automatic control tegulatingdevice according to claim 1, it is characterized in that: described unsaturated steam passage comprises unsaturated steam steam inlet valve (16), unsaturated steam pipeline (101), heating temperature-voltage monitor (18), heating equipment (17) and steam intensification steam inlet valve (19), unsaturated steam pipeline (101) is communicated with steam input pipe (1) and steam output pipe road (12), unsaturated steam steam inlet valve (16) is installed in unsaturated steam pipeline (101), heating equipment (17), heating temperature-voltage monitor (18) and steam intensification steam inlet valve (19), unsaturated steam steam inlet valve (16) connects input temperature-voltage monitor (3) by cable conductor, heating temperature-voltage monitor (18) connects respectively heating equipment (17) and steam intensification steam inlet valve (19) by cable conductor.
5. vapo(u)rous degree automatic control tegulatingdevice according to claim 4, is characterized in that: described heating equipment (17) is arranged between unsaturated steam steam inlet valve (16) and heating temperature-voltage monitor (18).
6. vapo(u)rous degree automatic control tegulatingdevice according to claim 1, it is characterized in that: described micro-superheated vapor passage comprises admission buffer (7), buffering temperature-voltage monitor (8) and steam buffer delivery valve (9), admission buffer (7) is arranged between steam input pipe (1) and steam output pipe road (12), upper buffering temperature-voltage monitor (8) and the drip pipe installed of admission buffer (7), admission buffer (7) rear portion connects steam buffer delivery valve (9), buffering temperature-voltage monitor (8) connects steam buffer delivery valve (9) by cable conductor.
7. vapo(u)rous degree automatic control tegulatingdevice according to claim 6, it is characterized in that: described drip pipe is arranged on admission buffer (7) bottom, condensed water elimination valve (20) is installed in drip pipe, and condensed water elimination valve (20) connects buffering temperature-voltage monitor (8) by cable conductor.
8. vapo(u)rous degree automatic control tegulatingdevice according to claim 6, is characterized in that: described steam buffer delivery valve (9) is arranged between admission buffer (7) and output temperature-voltage monitor (11).
9. vapo(u)rous degree automatic control tegulatingdevice according to claim 1, it is characterized in that: the described hot vapour passage that surpasses comprises superheated vapor suction valve (4), superheated vapor pipeline (102), cooling unit (13), cooling temperature-voltage monitor (14), cooling steam inlet valve (15) and admission buffer (7), superheated vapor pipeline (102) one end connects steam input pipe (1), the other end connects cooling unit (13), the upper cooling temperature-voltage monitor (14) of installing of cooling unit (13), cooling unit (13) connects admission buffer (7), cooling steam inlet valve (15) is installed between cooling unit (13) and admission buffer (7).
10. vapo(u)rous degree automatic control tegulatingdevice according to claim 9, is characterized in that: described cooling temperature-voltage monitor (14) connects cooling unit (13) by cable conductor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410404829.8A CN104180161B (en) | 2014-08-18 | 2014-08-18 | Automatic steam saturation degree adjusting device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410404829.8A CN104180161B (en) | 2014-08-18 | 2014-08-18 | Automatic steam saturation degree adjusting device |
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| Publication Number | Publication Date |
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| CN104180161A true CN104180161A (en) | 2014-12-03 |
| CN104180161B CN104180161B (en) | 2017-02-15 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201410404829.8A Active CN104180161B (en) | 2014-08-18 | 2014-08-18 | Automatic steam saturation degree adjusting device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105662833A (en) * | 2016-02-27 | 2016-06-15 | 彭盛华 | Fumigation physiotherapy equipment capable of being used in combination with closestool |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4099382A (en) * | 1976-06-21 | 1978-07-11 | Texaco Inc. | By-product superheated steam from the partial oxidation process |
| CN1419071A (en) * | 2002-12-16 | 2003-05-21 | 王逢旦 | Automatic controllable steam generator and method for generating steam |
| CN2660315Y (en) * | 2003-09-07 | 2004-12-01 | 曲景春 | High pureness steam producer |
| CN201463059U (en) * | 2009-08-07 | 2010-05-12 | 北京京诚科林环保科技有限公司 | Steam saturated system |
| CN204042442U (en) * | 2014-08-18 | 2014-12-24 | 山东新华医疗器械股份有限公司 | Vapo(u)rous degree automatic control tegulatingdevice |
-
2014
- 2014-08-18 CN CN201410404829.8A patent/CN104180161B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4099382A (en) * | 1976-06-21 | 1978-07-11 | Texaco Inc. | By-product superheated steam from the partial oxidation process |
| CN1419071A (en) * | 2002-12-16 | 2003-05-21 | 王逢旦 | Automatic controllable steam generator and method for generating steam |
| CN2660315Y (en) * | 2003-09-07 | 2004-12-01 | 曲景春 | High pureness steam producer |
| CN201463059U (en) * | 2009-08-07 | 2010-05-12 | 北京京诚科林环保科技有限公司 | Steam saturated system |
| CN204042442U (en) * | 2014-08-18 | 2014-12-24 | 山东新华医疗器械股份有限公司 | Vapo(u)rous degree automatic control tegulatingdevice |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105662833A (en) * | 2016-02-27 | 2016-06-15 | 彭盛华 | Fumigation physiotherapy equipment capable of being used in combination with closestool |
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| CN104180161B (en) | 2017-02-15 |
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