US20120291985A1 - Method of sensing abnormal condition in heat exchange process and heat exchange apparatus - Google Patents
Method of sensing abnormal condition in heat exchange process and heat exchange apparatus Download PDFInfo
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- US20120291985A1 US20120291985A1 US13/521,951 US201013521951A US2012291985A1 US 20120291985 A1 US20120291985 A1 US 20120291985A1 US 201013521951 A US201013521951 A US 201013521951A US 2012291985 A1 US2012291985 A1 US 2012291985A1
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- process fluid
- heat medium
- heat exchange
- sensing
- flow path
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- 238000000034 method Methods 0.000 title claims abstract description 121
- 230000002159 abnormal effect Effects 0.000 title claims abstract description 19
- 239000012530 fluid Substances 0.000 claims abstract description 76
- 150000003839 salts Chemical class 0.000 claims abstract description 52
- 239000012808 vapor phase Substances 0.000 claims abstract description 12
- 150000003333 secondary alcohols Chemical class 0.000 claims abstract description 8
- 238000000354 decomposition reaction Methods 0.000 claims abstract description 7
- IOVCWXUNBOPUCH-UHFFFAOYSA-M Nitrite anion Chemical compound [O-]N=O IOVCWXUNBOPUCH-UHFFFAOYSA-M 0.000 claims abstract description 6
- 229910002651 NO3 Inorganic materials 0.000 claims abstract description 5
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 claims abstract description 5
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 claims description 63
- 239000007789 gas Substances 0.000 claims description 63
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 15
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 13
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 13
- 239000001569 carbon dioxide Substances 0.000 claims description 12
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 12
- 230000008018 melting Effects 0.000 claims description 6
- 238000002844 melting Methods 0.000 claims description 6
- 239000001257 hydrogen Substances 0.000 claims description 5
- 229910052739 hydrogen Inorganic materials 0.000 claims description 5
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 2
- LPXPTNMVRIOKMN-UHFFFAOYSA-M sodium nitrite Chemical compound [Na+].[O-]N=O LPXPTNMVRIOKMN-UHFFFAOYSA-M 0.000 description 28
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 27
- JMSUNAQVHOHLMX-UHFFFAOYSA-N 1-cyclohexylethanol Chemical compound CC(O)C1CCCCC1 JMSUNAQVHOHLMX-UHFFFAOYSA-N 0.000 description 20
- LDLDYFCCDKENPD-UHFFFAOYSA-N ethenylcyclohexane Chemical group C=CC1CCCCC1 LDLDYFCCDKENPD-UHFFFAOYSA-N 0.000 description 19
- 239000000203 mixture Substances 0.000 description 14
- 229910052757 nitrogen Inorganic materials 0.000 description 13
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 13
- 229910001220 stainless steel Inorganic materials 0.000 description 12
- 239000010935 stainless steel Substances 0.000 description 12
- 238000010521 absorption reaction Methods 0.000 description 11
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 10
- 230000018044 dehydration Effects 0.000 description 5
- 238000006297 dehydration reaction Methods 0.000 description 5
- 239000011521 glass Substances 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 229920002313 fluoropolymer Polymers 0.000 description 3
- 150000002431 hydrogen Chemical class 0.000 description 3
- 239000007791 liquid phase Substances 0.000 description 3
- 238000005070 sampling Methods 0.000 description 3
- 235000010288 sodium nitrite Nutrition 0.000 description 3
- 238000012795 verification Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- LPLLVINFLBSFRP-UHFFFAOYSA-N 2-methylamino-1-phenylpropan-1-one Chemical compound CNC(C)C(=O)C1=CC=CC=C1 LPLLVINFLBSFRP-UHFFFAOYSA-N 0.000 description 2
- 241000132539 Cosmos Species 0.000 description 2
- 235000005956 Cosmos caudatus Nutrition 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 238000005868 electrolysis reaction Methods 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- LGAQJENWWYGFSN-PLNGDYQASA-N (z)-4-methylpent-2-ene Chemical compound C\C=C/C(C)C LGAQJENWWYGFSN-PLNGDYQASA-N 0.000 description 1
- WVYWICLMDOOCFB-UHFFFAOYSA-N 4-methyl-2-pentanol Chemical compound CC(C)CC(C)O WVYWICLMDOOCFB-UHFFFAOYSA-N 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 238000004255 ion exchange chromatography Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000004323 potassium nitrate Substances 0.000 description 1
- 235000010333 potassium nitrate Nutrition 0.000 description 1
- 239000004317 sodium nitrate Substances 0.000 description 1
- 235000010344 sodium nitrate Nutrition 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Images
Classifications
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01M—TESTING STATIC OR DYNAMIC BALANCE OF MACHINES OR STRUCTURES; TESTING OF STRUCTURES OR APPARATUS, NOT OTHERWISE PROVIDED FOR
- G01M3/00—Investigating fluid-tightness of structures
- G01M3/02—Investigating fluid-tightness of structures by using fluid or vacuum
- G01M3/04—Investigating fluid-tightness of structures by using fluid or vacuum by detecting the presence of fluid at the leakage point
- G01M3/20—Investigating fluid-tightness of structures by using fluid or vacuum by detecting the presence of fluid at the leakage point using special tracer materials, e.g. dye, fluorescent material, radioactive material
- G01M3/22—Investigating fluid-tightness of structures by using fluid or vacuum by detecting the presence of fluid at the leakage point using special tracer materials, e.g. dye, fluorescent material, radioactive material for pipes, cables or tubes; for pipe joints or seals; for valves; for welds; for containers, e.g. radiators
- G01M3/226—Investigating fluid-tightness of structures by using fluid or vacuum by detecting the presence of fluid at the leakage point using special tracer materials, e.g. dye, fluorescent material, radioactive material for pipes, cables or tubes; for pipe joints or seals; for valves; for welds; for containers, e.g. radiators for containers, e.g. radiators
- G01M3/228—Investigating fluid-tightness of structures by using fluid or vacuum by detecting the presence of fluid at the leakage point using special tracer materials, e.g. dye, fluorescent material, radioactive material for pipes, cables or tubes; for pipe joints or seals; for valves; for welds; for containers, e.g. radiators for containers, e.g. radiators for radiators
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01M—TESTING STATIC OR DYNAMIC BALANCE OF MACHINES OR STRUCTURES; TESTING OF STRUCTURES OR APPARATUS, NOT OTHERWISE PROVIDED FOR
- G01M3/00—Investigating fluid-tightness of structures
- G01M3/02—Investigating fluid-tightness of structures by using fluid or vacuum
- G01M3/04—Investigating fluid-tightness of structures by using fluid or vacuum by detecting the presence of fluid at the leakage point
- G01M3/20—Investigating fluid-tightness of structures by using fluid or vacuum by detecting the presence of fluid at the leakage point using special tracer materials, e.g. dye, fluorescent material, radioactive material
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F27/00—Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01M—TESTING STATIC OR DYNAMIC BALANCE OF MACHINES OR STRUCTURES; TESTING OF STRUCTURES OR APPARATUS, NOT OTHERWISE PROVIDED FOR
- G01M3/00—Investigating fluid-tightness of structures
- G01M3/02—Investigating fluid-tightness of structures by using fluid or vacuum
- G01M3/04—Investigating fluid-tightness of structures by using fluid or vacuum by detecting the presence of fluid at the leakage point
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2265/00—Safety or protection arrangements; Arrangements for preventing malfunction
- F28F2265/16—Safety or protection arrangements; Arrangements for preventing malfunction for preventing leakage
Landscapes
- Physics & Mathematics (AREA)
- Engineering & Computer Science (AREA)
- General Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Investigating Or Analyzing Non-Biological Materials By The Use Of Chemical Means (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Examining Or Testing Airtightness (AREA)
Abstract
A method of sensing an abnormal condition in a heat exchange process, capable of promptly and readily sensing leakage of a heat medium into a process fluid flow path in a process of heat exchange, is provided. The present invention is directed to a method of sensing an abnormal condition in a heat exchange process between the heat medium and the process fluid having a sensing step of sensing a gas component generated as a result of decomposition of a heat medium and/or a gas component generated as a result of contact between the heat medium and the process fluid, in a vapor phase portion in a flow path for the process fluid. The method is preferably applied in a heat exchange process where the heat medium is fused salt including nitrate and/or nitrite and the process fluid includes secondary alcohols or a dehydrated product thereof.
Description
- The present invention relates to a method of sensing an abnormal condition in a process of heat exchange between a heat medium and a process fluid and a heat exchange apparatus of which abnormal condition is sensed with the method of sensing an abnormal condition.
- In a heat exchange process, fused salt, water, or the like is employed as a heat medium, and a temperature of a process fluid is adjusted to a prescribed temperature as a result of heat exchange between this heat medium and the process fluid. For example, fused salt which is a mixture such as sodium nitrite and potassium nitrate has such properties as (1) excellent heat conduction capability, (2) high chemical stability even at a high temperature, and (3) ease in temperature control. Therefore, fused salt has been used as a high temperature heat medium for heating or cooling various process fluids.
- During the heat exchange process, a process fluid or a heat medium may leak due to corrosion or the like of a pipe and a method of sensing leakage of a fluid has been studied. For example, Japanese Patent Laying-Open No. 2003-82833 (PTL 1) has proposed a method of sensing a gas component (nitrogen oxide) generated at the time when a leaked process fluid reacts to a heat medium, in a vapor phase portion in a flow path for the heat medium.
- PTL 1: Japanese Patent Laying-Open No. 2003-83833
- With the method described in PTL 1, however, leakage of a heat medium into a process fluid flow path cannot be sensed, and there has been a possibility of occurrence of a secondary disaster such as explosion.
- It is an object of the present invention is to provide a method of sensing an abnormal condition in a heat exchange process, capable of promptly sensing leakage of a heat medium into a flow path for a process fluid. In addition, it is also an object to provide a heat exchange apparatus of which abnormal condition is sensed with such a method of sensing an abnormal condition.
- The present invention provides a method of sensing an abnormal condition in a heat exchange process for heat exchange between a heat medium and a process fluid, having a sensing step of sensing a gas component generated as a result of decomposition of the heat medium and/or a gas component generated as a result of contact between the heat medium and the process fluid, in a vapor phase portion in a flow path for the process fluid. In the sensing step, leakage of a heat medium into a process fluid flow path can promptly and readily be sensed.
- The method of sensing an abnormal condition according to the present invention described above is preferably used in a heat exchange process, in which the heat medium is fused salt including nitrate and/or nitrite and the process fluid contains secondary alcohols and/or a dehydrated product thereof. In this case, the gas component sensed in the sensing step includes, for example, at least one of nitrogen oxide (NOx), carbon monoxide (CO), carbon dioxide (CO2), and hydrogen (H2).
- The method of sensing an abnormal condition according to the present invention described above is further preferably used in a heat exchange process, in which the heat medium is fused salt including nitrate and 20 to 90 weight % of nitrite and having a melting point from 100 to 200° C. Namely, in the case where the heat medium is the fused salt including nitrite such as sodium nitrite (NaNO2), since at least one of nitrogen oxide, carbon monoxide, carbon dioxide, and hydrogen is generated as a result of reaction between this heat medium and the process fluid, leakage of the process fluid can promptly be sensed by sensing this gas.
- In addition, the present invention provides a heat exchange apparatus including a process fluid flow path through which a process fluid flows, a heat medium flow path through which a heat medium flows, a heat exchanger for heat exchange between the heat medium and the process fluid, and a gas sensor for sensing a gas component generated as a result of decomposition of the heat medium and/or a gas component generated as a result of contact between the heat medium and the process fluid, the gas sensor being provided in a vapor phase portion in the process fluid flow path.
- It is noted that the “heat exchange process” in the present invention is a concept encompassing also a dehydration process of secondary alcohols.
- According to the method of sensing an abnormal condition in a heat exchange process or the heat exchange apparatus in the present invention, in a heat exchange process for heat exchange between a heat medium and a process fluid, leakage of a heat medium can promptly and readily be sensed by sensing a gas component generated as a result of decomposition of the heat medium and/or a gas component generated as a result of contact between the heat medium and the process fluid, in a vapor phase portion in a flow path for the process fluid.
-
FIG. 1 is a schematic diagram showing one embodiment of a heat exchange apparatus according to the present invention. -
FIG. 2 is a schematic diagram showing a test apparatus used in a verification test according to the present invention. - The present invention will be described hereinafter in detail with reference to the drawings.
FIG. 1 is a schematic diagram showing one embodiment of a heat exchange apparatus according to the present invention. In the heat exchange apparatus shown inFIG. 1 , an abnormal condition of leakage of a heat medium is sensed with the method of sensing an abnormal condition according to the present invention. - The heat exchange apparatus shown in
FIG. 1 includes a process fluid flow path through which a process fluid flows, a heat medium flow path through which a heat medium flows, a heat exchanger 1 for heat exchange between the heat medium and the process fluid, and agas sensor 4 for sensing a gas component generated as a result of decomposition of the heat medium and/or a gas component generated as a result of contact between the heat medium and the process fluid. - The process fluid is supplied to heat exchanger 1 through a
pipe 2. In the present embodiment, the process fluid flow path means a flow path from a conduit in heat exchanger 1 to anabsorption tower 12 through which a process fluid flows and a flow path branched therefrom (for example, a circulating path, a vent line). Therefore, the process fluid flow path includes heat exchanger 1 andabsorption tower 12, as well aspipes cooler 17, and avent line 16 ofabsorption tower 12. A fluid flow path subsequent toabsorption tower 12 is not included. The gas sensor should only be provided in a vapor phase portion in the process fluid flow path. In the present embodiment,gas sensor 4 is provided inpipe 3 branched frompipe 11 connecting heat exchanger 1 andabsorption tower 12 to each other.Gas sensor 4 can also be provided invent line 16 ofabsorption tower 12. In the present embodiment, anNO sensor 14 is further provided in apipe 13 branched fromvent line 16 ofabsorption tower 12. - In the present embodiment, the heat medium flow path means a flow path including heat exchanger 1, a
pipe 5, aheat medium tank 6, a pump 9, and a cooler andheater 10, and a flow path branched therefrom (for example, a circulating path, a vent line). - In the heat exchange apparatus shown in
FIG. 1 ,gas sensor 4 orNO sensor 14 senses a decomposed gas component of the heat medium which leaked into the process fluid flow path in heat exchanger 1 and/or a gas component generated as a result of contact of the heat medium which leaked into the process fluid flow path with the process fluid. - Heat exchanger 1 is not particularly limited so long as heat exchange between a process fluid and a heat medium is achieved with a partition wall such as a pipe or a flat plate being interposed, and for example, a shell-and-tube cylindrical heat exchanger, a plate-type heat exchanger, a spiral heat exchanger, a block heat exchanger, or the like representing a bulkhead heat exchanger can be employed. The heat exchanger includes not only a heat exchanger simply for heat exchange but also a reactor such as a multi-tubular catalytic packed reactor for heat exchange and reaction.
- Preferably, fused salt, water, or the like is employed as the heat medium. As this fused salt, a composition containing 20 to 90 weight % of sodium nitrite (NaNO2) having a melting point in a range approximately from 100 to 200° C. is preferred. In the case where a composition composed of NaNO2, sodium nitrate (NaNO3), and potassium nitrate (KNO3) is employed as fused salt, fused salt containing these components in ranges from 20 to 50 weight %, from 5 to 15 weight %, and from 45 to 65 weight %, respectively, is more preferred. Alternatively, in the case where a composition composed of NaNO2 and KNO3 is employed as fused salt, fused salt containing these components in ranges from 20 to 90 weight % and from 80 to 10 weight %, respectively, is more preferred. Specifically, for example, a composition composed of NaNO2 (40 weight %), NaNO3 (7 weight %), and KNO3 (53 weight %) (having a melting point of 142° C.), a composition composed of NaNO2 (34 weight %), NaNO3 (13 weight %), and KNO3 (53 weight %) (having a melting point of 152° C.), a composition composed of NaNO2 (50 weight %) and KNO3 (50 weight %) (having a melting point of 139° C.), and the like are exemplified. In order to lower a freezing point of these fused salts and facilitate temperature control, water may be added for use.
- The process fluid is not particularly limited so long as a process fluid can generate a gas as a result of contact with a heat medium when the heat medium flows into the process fluid flow path and that gas can be sensed in the vapor phase portion in the process fluid flow path. For example, a property of the process fluid may be any of a solid, a liquid, and a gas, however, a gas is desirable.
- In the case where fused salt is employed as the heat medium, for example, a process fluid including various secondary alcohols and/or a dehydrated product thereof is preferred as the process fluid. Specifically, for example, a process fluid including methylcyclohexyl carbinol (MCC) representing a secondary alcohol or cyclohexyl ethylene (CHE) representing a dehydrated product thereof, and the like are exemplified.
- In addition, as the process fluid, for example, a process fluid including 4-methyl-2-pentanol representing a secondary alcohol or 4-methyl-2-pentene representing a dehydrated product thereof, and the like are exemplified. When these process fluids and fused salt come in contact with each other, NOx, CO, CO2, H2, or the like is generated.
- A dehydration process (one type of a heat exchange process) in which fused salt is employed as the heat medium, MCC is employed as the process fluid, and CHE is generated by dehydrating this MCC will be described hereinafter in detail.
- Namely, MCC is introduced in heat exchanger 1 (reactor) through
pipe 2, heat exchange between MCC and fused salt approximately from 300 to 400° C. is carried out in heat exchanger 1, CHE is generated from MCC as a result of dehydration through vapor phase reaction, and CHE is sent throughpipe 11 andcooler 17 toabsorption tower 12. A CHE solution that enteredabsorption tower 12 is circulated by apump 15, and a part thereof is used as an absorbing solution and a part thereof is guided to downstream of a process. - Fused salt that has completed heat exchange with the process fluid is discharged from heat exchanger 1 and sent to
heat medium tank 6 throughpipe 5. A prescribed amount of fused salt is stored in thisheat medium tank 6, andheat medium tank 6 is constituted of a liquid phase portion 7 (fused salt) and avapor phase portion 8. Fused salt inliquid phase portion 7 is sent by pump 9 to cooler andheater 10 for heating and/or cooling this fused salt, cooled or heated, and thereafter again supplied to heat exchanger 1. - Since the aforementioned dehydration process of the secondary alcohols is generally performed substantially at an atmospheric pressure, the process fluid flow path is maintained at a pressure lower than that in the heat medium flow path. Therefore, when a crack or the like is produced due to stress or corrosion in the process fluid flow path (partition wall) in heat exchanger 1 during the dehydration process, fused salt leaks into the process fluid flow path and reacts to the process fluid, and hence NOx, CO, CO2, H2, or the like is generated. Furthermore, a gas component (NOx or the like) generated as a result of thermal decomposition of fused salt may also flow into the process fluid flow path.
- By having the sensing step of sensing these gas components with
gas sensor 4 or NOxsensor 14, leakage of the heat medium is sensed in an early stage. Thus, an interlock can be activated so that supply of the process fluid and fused salt into heat exchanger 1 is stopped and damage can be prevented from expanding. - As
gas sensor 4, a controlled-potential electrolysis type or infrared type NOx sensor, an infrared absorption type CO/CO2 sensor, a contact combustion type hydrogen sensor, and the like can be employed. Specifically, a controlled-potential electrolysis type NOx meter manufactured by New Cosmos Electric Co., Ltd., an infrared type gas analyzer manufactured by Yokogawa Electric Corporation, a contact combustion type hydrogen sensor manufactured by New Cosmos Electric Co., Ltd., and the like are exemplified. - A verification test for verifying that the method of sensing an abnormal condition according to the present invention is effective was conducted in the following.
-
FIG. 2 shows a schematic diagram of an overall test apparatus used in the verification test. With the use of this test apparatus, a gas generated at the time when fused salt containing NaNO2 and a process fluid containing MCC or CHE were mixed was evaluated. - In the test apparatus shown in
FIG. 2 , athermostatic bath 21 contains astainless steel vessel 22 for evaluating risk of mixture of fused salt and an introduced gas, fusedsalt 23 placed instainless steel vessel 22, asupply pipe 35 for supplying an introduced gas including an MCC gas or a CHE gas to fusedsalt 23 withinvessel 22, and a fusedsalt collection vessel 34 for preventing fusedsalt 23 from flowing back to upstream of the apparatus. Apipe 24 for collecting an exhaust gas is attached tostainless steel vessel 22. The exhaust gas is cooled in aglass vessel 26 immersed in a cooler 25 and a part thereof is collected in afluoroplastic sampling bag 28 through apipe 27. - The introduced gas is prepared by bubbling an N2 gas supplied from an N2 cylinder 29 into a
glass vessel 31 containing a process fluid 32 (MCC or CHE) heated in anoil bath 33. In addition, by heating a pipe betweenglass vessel 31 and fusedsalt collection vessel 34 to a temperature not lower than a boiling point of MCC or CHE by using aribbon heater 36, the introduced gas can be prevented from condensing in the pipe. A flow rate of a gas from N2 cylinder 29 is adjusted by agas flowmeter 30. It is noted that T represents a temperature sensor inFIG. 2 . - Tests 1 to 6 were conducted in the following procedures by using the test apparatus as above. It is noted that, in
Tests - (1) Ten grams of fused salt (NaNO2:40 weight %, NaNO3:7 weight %, KNO3:53 weight %) were loaded in 150 ml
stainless steel vessel 22. - (2)
Stainless steel vessel 22 was placed inthermostatic bath 21 and heated to an isothermal temperature of 380° C. - (3) After fused salt reached a prescribed temperature, a line from N2 cylinder 29 to
pipe 27 through which an exhaust gas passed was substituted with a nitrogen gas. - (4) A gas mixture of MCC and nitrogen (Tests 3, 4), a gas mixture of CHE and nitrogen (Tests 5, 6), or nitrogen alone (Tests 1, 2) was supplied to
stainless steel vessel 22 at a flow rate of approximately 2000 mL/min. - (5) A gas generated as a result of supply of the gas mixture of MCC and nitrogen, the gas mixture of CHE and nitrogen, or nitrogen alone was collected in
fluoroplastic sampling bag 28 for a prescribed period of time. - (6) Of the collected exhaust gas, NOx was measured with ion chromatography and other gases were measured with gas chromatography, and volumetric composition of the exhaust gas was examined. Table 1 shows test results.
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TABLE 1 Amount of Loaded Composition of Exhaust Gas Fused [Vol %] Salt [g] Type of Fed Gas H2 CO CO2 NOx Test 1 0 Nitrogen <0.1 0.0009 0.043 0.0033 Test 210 Nitrogen <0.1 0.0003 0.034 0.019 Test 30 Nitrogen, MCC 0.3 0.0046 0.05 0.010 Test 410 Nitrogen, MCC 1.4 0.032 0.36 0.044 Test 50 Nitrogen, CHE 5.3 0.036 0.37 0.0010 Test 610 Nitrogen, CHE 13.7 0.028 0.20 0.024 - As shown in Table 1, it was found from Test 1 conducted for comparison (where no fused salt was loaded but nitrogen alone was fed) that H2, CO, CO2, and NOx could be regarded as not existing in the test apparatus. It was found that, in
Test 2, fused salt was heated to 380° C. instainless steel vessel 22, increase in NOx was observed as compared with Test 1, and hence fused salt locally decomposed at that temperature. InTest 3, MCC was heated to 380° C. instainless steel vessel 22, and H2, CO, and NOx increased as compared with Test 1. Therefore, it was found that, under such conditions, MCC locally decomposed. - In
Test 4, heating to 380° C. was carried out while MCC and fused salt were in contact with each other instainless steel vessel 22, and as compared withTests Test 5, CHE was heated to 380° C. instainless steel vessel 22, and as compared with Test 1, H2, CO, and CO2 increased. Therefore, it was found that, under such conditions, CHE locally decomposed. InTest 6, heating to 380° C. was carried out while CHE and fused salt were in contact with each other instainless steel vessel 22, and as compared withTests - 1 heat exchanger; 2 pipe; 3 pipe; 4 gas sensor; 5 pipe; 6 heat medium tank; 7 liquid phase portion; 8 vapor phase portion; 9 pump; 10 cooler and heater; 11 pipe; 12 absorption tower; 13 pipe; 14 NOx sensor; 15 pump; 16 vent line; 17 cooler; 21 thermostatic bath; 22 stainless steel vessel; 23 fused salt; 24 pipe; 25 cooler; 26 glass vessel; 27 pipe; 28 fluoroplastic sampling bag; 29 N2 cylinder; 30 gas flowmeter; 31 glass vessel; 32 process fluid (MCC or CHE); 33 oil bath; 34 fused salt collection vessel; 35 supply pipe; and 36 ribbon heater.
Claims (4)
1. A method of sensing an abnormal condition in a heat exchange process for heat exchange between a heat medium and a process fluid, comprising:
a sensing step of sensing a gas component generated as a result of decomposition of said heat medium and/or a gas component generated as a result of contact between said heat medium and said process fluid, in a vapor phase portion in a flow path for said process fluid.
2. The method of sensing an abnormal condition in a heat exchange process according to claim 1 , wherein
said heat medium is fused salt including nitrate and/or nitrite,
said process fluid contains secondary alcohols and/or a dehydrated product thereof, and
said gas component sensed in said sensing step includes at least one of nitrogen oxide, carbon monoxide, carbon dioxide, and hydrogen.
3. The method of sensing an abnormal condition in a heat exchange process according to claim 2 , wherein
said fused salt includes said nitrate and 20 to 90 weight % of said nitrite and has a melting point from 100 to 200° C.
4. A heat exchange apparatus, comprising:
a process fluid flow path through which a process fluid flows;
a heat medium flow path through which a heat medium flows;
a heat exchanger for heat exchange between said heat medium and said process fluid; and
a gas sensor for sensing a gas component generated as a result of decomposition of said heat medium and/or a gas component generated as a result of contact between said heat medium and said process fluid,
said gas sensor being provided in a vapor phase portion in said process fluid flow path.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
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JP2010-004813 | 2010-01-13 | ||
JP2010004813A JP2011145126A (en) | 2010-01-13 | 2010-01-13 | Abnormality detection method of heat exchange process |
PCT/JP2010/073712 WO2011086853A1 (en) | 2010-01-13 | 2010-12-28 | Method for detecting abnormality in heat-exchange process, and heat exchanger |
Publications (1)
Publication Number | Publication Date |
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US20120291985A1 true US20120291985A1 (en) | 2012-11-22 |
Family
ID=44304135
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US13/521,951 Abandoned US20120291985A1 (en) | 2010-01-13 | 2010-12-28 | Method of sensing abnormal condition in heat exchange process and heat exchange apparatus |
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US (1) | US20120291985A1 (en) |
EP (1) | EP2525204A1 (en) |
JP (1) | JP2011145126A (en) |
KR (1) | KR20120125295A (en) |
CN (1) | CN102713553A (en) |
SG (1) | SG182441A1 (en) |
WO (1) | WO2011086853A1 (en) |
Cited By (1)
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US10974590B2 (en) | 2015-06-22 | 2021-04-13 | Ford Global Technologies, Llc | Fuel tank baffle with pivotable vanes |
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CN108692868A (en) * | 2017-04-10 | 2018-10-23 | 中国石油天然气股份有限公司 | Water cooling heat exchanger cools down medium leakage inspection method |
CN108776025B (en) * | 2018-06-11 | 2020-07-31 | 江西江铃集团新能源汽车有限公司 | Thermal management system test platform of electric drive system |
Family Cites Families (11)
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DE1501531B2 (en) * | 1965-09-22 | 1971-12-02 | Kabel- und Metallwerke Gutehoffnungshütte AG, 3000 Hannover | MULTILAYER HEAT EXCHANGER TUBE AND USE OF THE SAME 1 |
JPS5625968B2 (en) * | 1975-02-21 | 1981-06-16 | ||
US4090554A (en) * | 1976-11-17 | 1978-05-23 | The Babcock & Wilcox Company | Heat exchanger |
JPS5396375A (en) * | 1977-02-01 | 1978-08-23 | Miura Harunobu | Skin peeling method of fruit and vwgetable |
US6293104B1 (en) * | 1999-05-17 | 2001-09-25 | Hitachi, Ltd. | Condenser, power plant equipment and power plant operation method |
JP4665283B2 (en) * | 2000-03-06 | 2011-04-06 | トヨタ自動車株式会社 | Heat exchange system |
JP2002153745A (en) * | 2000-11-15 | 2002-05-28 | National Institute Of Advanced Industrial & Technology | Method for utilizing heat of combustion of biomass alcohol and system therefor |
TW534972B (en) * | 2001-06-26 | 2003-06-01 | Sumitomo Chemical Co | Method and device for detecting abnormality in process for exchanging heat |
JP2003083833A (en) * | 2001-06-26 | 2003-03-19 | Sumitomo Chem Co Ltd | Abnormality detection method of heat exchanging process |
JP2003082833A (en) | 2001-09-12 | 2003-03-19 | Yamamoto Yogyo Kako Co Ltd | Method and structure for finishing projected corner part |
TW200902151A (en) * | 2007-02-12 | 2009-01-16 | Basf Ag | Method for leakage monitoring in a tube bundle reactor |
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2010
- 2010-01-13 JP JP2010004813A patent/JP2011145126A/en active Pending
- 2010-12-28 EP EP10843205A patent/EP2525204A1/en not_active Withdrawn
- 2010-12-28 CN CN201080061084XA patent/CN102713553A/en active Pending
- 2010-12-28 KR KR1020127021089A patent/KR20120125295A/en not_active Application Discontinuation
- 2010-12-28 WO PCT/JP2010/073712 patent/WO2011086853A1/en active Application Filing
- 2010-12-28 US US13/521,951 patent/US20120291985A1/en not_active Abandoned
- 2010-12-28 SG SG2012050712A patent/SG182441A1/en unknown
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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US10974590B2 (en) | 2015-06-22 | 2021-04-13 | Ford Global Technologies, Llc | Fuel tank baffle with pivotable vanes |
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SG182441A1 (en) | 2012-08-30 |
CN102713553A (en) | 2012-10-03 |
JP2011145126A (en) | 2011-07-28 |
WO2011086853A1 (en) | 2011-07-21 |
EP2525204A1 (en) | 2012-11-21 |
KR20120125295A (en) | 2012-11-14 |
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