CN202204791U - Heat transfer coefficient determining device for heat exchange tube of heating furnace - Google Patents

Heat transfer coefficient determining device for heat exchange tube of heating furnace Download PDF

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Publication number
CN202204791U
CN202204791U CN2011203244512U CN201120324451U CN202204791U CN 202204791 U CN202204791 U CN 202204791U CN 2011203244512 U CN2011203244512 U CN 2011203244512U CN 201120324451 U CN201120324451 U CN 201120324451U CN 202204791 U CN202204791 U CN 202204791U
Authority
CN
China
Prior art keywords
transfer coefficient
heat transfer
heating furnace
water tank
heat exchange
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN2011203244512U
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Chinese (zh)
Inventor
杨渠忠
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
TAINJIN PETROLEUM MODERN OIL EQUIPMENT CO Ltd
Original Assignee
TAINJIN PETROLEUM MODERN OIL EQUIPMENT CO Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by TAINJIN PETROLEUM MODERN OIL EQUIPMENT CO Ltd filed Critical TAINJIN PETROLEUM MODERN OIL EQUIPMENT CO Ltd
Priority to CN2011203244512U priority Critical patent/CN202204791U/en
Application granted granted Critical
Publication of CN202204791U publication Critical patent/CN202204791U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to a heat transfer coefficient determining device for a heat exchange tube of a heating furnace, which comprises a water tank, wherein a water filling opening is arranged on the water tank, an electric heater and a coiler pipe are arranged in the water tank, the inlet end and the outlet end of the coiler pipe extend to the outside of the water tank, a thermometer and a pressure gage are arranged at both the inlet end and the outlet end of the coiler pipe, and a flow meter is arranged at the input end or the output end. The heat transfer coefficient determining device can determine heat transfer coefficient of the heat exchange tube of the heating furnace through tests. Data is obtained through tests operated by using the device, and the heat transfer coefficient of the heat exchange tube of the heating furnace is determined through calculation. The heat transfer coefficient determining device is small in error and high in accuracy, is used for designing the practical heat exchange area of the heat exchange tube of the heating furnace, and is more accurate.

Description

Heating furnace heat exchanger tube heat transfer coefficient determinator
Technical field
The utility model relates to a kind of heating furnace heat exchanger tube heat transfer coefficient determinator, is used for the mensuration of the heat transfer coefficient of oil field heating furnace coil pipe.
Background technology
Some oil field is higher because of the heavy constituent content in crude oil or the rock gas, needs to adopt heating furnace that crude oil or rock gas are heated up.Heat exchanger tube heat transfer coefficient determinator is exclusively used in the mensuration to heating furnace coil pipe heat transfer coefficient.The design of oil field heating furnace heat interchanging area, the necessary heat transfer coefficient of confirming heat exchanger tube earlier.Usually confirm heat transfer coefficient according to Theoretical Calculation and some empirical values earlier, calculate the heat transfer area of heat exchanger tube then according to heat transfer coefficient.But because block various oil property othernesses in oil field are very big, the heat interchanging area that the heat transfer coefficient of confirming through Theoretical Calculation or experience obtains is often not really accurate, often produces bigger deviation and can't satisfy the actual needs to crude oil or rock gas heating.
Summary of the invention
The purpose of the utility model provides a kind of heating furnace heat exchanger tube heat transfer coefficient determinator, can confirm the heat transfer coefficient of heating furnace heat exchanger tube through test with this device.
This heat transfer coefficient determinator comprises water tank, and water tank is provided with the filler; Electric heater and coil pipe are housed in the water tank, and the entrance point of coil pipe and endpiece extend to outside the water tank, and the entrance point of said coil pipe and endpiece all are equipped with thermometer and tensimeter, and entrance point or endpiece are equipped with flowmeter.
Said water tank is provided with blow vent.
Said water tank is provided with sewage draining exit and blowoff valve.
Said filler is provided with water valve.
Adopting this device is intermediate medium with the water in the water tank; Through electric heater water is heated, hot water is medium heating in the coil pipe, and the import and export temperature and the flow that record according to medium; Again according to the known heat transfer area and the power of electric heater, through formula calculate heat transfer coefficient.With the data that this device makes an experiment and obtains, through calculating the heat transfer coefficient of confirming the heating furnace heat exchanger tube, error is little again, and accuracy is high.Design the heat interchanging area of the reality of heating furnace heat exchanger tube with this heat transfer coefficient, more tally with the actual situation, avoid occurring the heating furnace too big problem of not enough or rich amount of exerting oneself.
Description of drawings
Fig. 1 is a heating furnace heat exchanger tube heat transfer coefficient determinator synoptic diagram
Figure acceptance of the bid is kept the score not Biao Shi be as follows:
1, media outlet, 2, the medium import, 3, the outlet temperature meter, 4, delivery gauge; 5, radiator thermometer, 6, filler and water valve, 7, blow vent, 8, coil pipe; 9, rate-of flow meter, 10, the inlet temperature meter, 11, inlet pressure gauge, 12, water; 13 water tanks, 14, blowoff valve, 15, electric heater.
Embodiment
Fig. 1 is hot stove heat exchanger tube heat transfer coefficient assay device structures synoptic diagram.Like Fig. 1, in water tank 13, add entry 12 from filler 6, simultaneously measured medium (crude oil or rock gas) is got into coil pipe 8 from import 2, flow out from media outlet 1.Water 12 in the water tank by electric heater 15 heating, with treat measured medium in heat transferred coil pipe 8, makes medium heat temperature raising after water is heated as intermediate medium.
From radiator thermometer 5 read the temperature data of water; Record the out temperature of measured medium respectively through inlet temperature meter 10, outlet temperature meter 3, inlet pressure gauge 11 and delivery gauge 4, rate-of flow meter 9; Inlet and outlet pressure and flow according to these parameters that records, calculate with formula K=Q/ (A* Δ Tm); (Q is a thermal power in the formula, can try to achieve according to electrical bar power and efficient to obtain the heat transfer coefficient of test unit.A is the actual heat interchanging area of coil pipe, can survey, and Δ Tm is a log-mean temperature difference).The K value that calculates is the heat transfer coefficient value.
In this device, blowoff valve 14 plays the blowdown effect, and blow vent 7 and atmosphere make to keep normal pressure in the water tank 13.

Claims (4)

1. heating furnace heat exchanger tube heat transfer coefficient determinator is characterized in that comprising water tank, and water tank is provided with the filler; Electric heater and coil pipe are housed in the water tank, and the entrance point of coil pipe and endpiece extend to outside the water tank, and the entrance point of said coil pipe and endpiece all are equipped with thermometer and tensimeter, and entrance point or endpiece are equipped with flowmeter.
2. heating furnace heat exchanger tube heat transfer coefficient determinator according to claim 1 is characterized in that said water tank is provided with blow vent.
3. heating furnace heat exchanger tube heat transfer coefficient determinator according to claim 2 is characterized in that said water tank is provided with sewage draining exit and blowoff valve.
4. heating furnace heat exchanger tube heat transfer coefficient determinator according to claim 3 is characterized in that said filler is provided with water valve.
CN2011203244512U 2011-08-31 2011-08-31 Heat transfer coefficient determining device for heat exchange tube of heating furnace Expired - Fee Related CN202204791U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011203244512U CN202204791U (en) 2011-08-31 2011-08-31 Heat transfer coefficient determining device for heat exchange tube of heating furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011203244512U CN202204791U (en) 2011-08-31 2011-08-31 Heat transfer coefficient determining device for heat exchange tube of heating furnace

Publications (1)

Publication Number Publication Date
CN202204791U true CN202204791U (en) 2012-04-25

Family

ID=45968909

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011203244512U Expired - Fee Related CN202204791U (en) 2011-08-31 2011-08-31 Heat transfer coefficient determining device for heat exchange tube of heating furnace

Country Status (1)

Country Link
CN (1) CN202204791U (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103499506A (en) * 2013-10-12 2014-01-08 天津市天塑科技集团有限公司技术中心 Simulation test bench for thermal power generation boiler fluoroplastic economizers
CN103675016A (en) * 2012-09-04 2014-03-26 华东理工大学 Testing system for phase change heating and temperature controlling effects of heat release type tubular reactor
CN104819993A (en) * 2015-05-18 2015-08-05 河海大学 Device and method for testing heat exchange coefficient of cooling water pipe walls
CN110376239A (en) * 2019-05-20 2019-10-25 西安交通大学 The quantitative measurement method of grease working medium shell-and-tube heat exchanger efficiency
CN114252475A (en) * 2020-09-22 2022-03-29 宝山钢铁股份有限公司 Method for checking efficiency of heat exchanger

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103675016A (en) * 2012-09-04 2014-03-26 华东理工大学 Testing system for phase change heating and temperature controlling effects of heat release type tubular reactor
CN103675016B (en) * 2012-09-04 2016-04-06 华东理工大学 The test macro of a kind of release type tubular reactor phase transformation heat-obtaining and temperature control effect
CN103499506A (en) * 2013-10-12 2014-01-08 天津市天塑科技集团有限公司技术中心 Simulation test bench for thermal power generation boiler fluoroplastic economizers
CN103499506B (en) * 2013-10-12 2016-07-06 天津市天塑科技集团有限公司技术中心 Thermal power generation boiler fluoroplastics economizer simulation test stand
CN104819993A (en) * 2015-05-18 2015-08-05 河海大学 Device and method for testing heat exchange coefficient of cooling water pipe walls
CN110376239A (en) * 2019-05-20 2019-10-25 西安交通大学 The quantitative measurement method of grease working medium shell-and-tube heat exchanger efficiency
CN114252475A (en) * 2020-09-22 2022-03-29 宝山钢铁股份有限公司 Method for checking efficiency of heat exchanger
CN114252475B (en) * 2020-09-22 2023-10-17 宝山钢铁股份有限公司 Method for verifying efficiency of heat exchanger

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Legal Events

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C14 Grant of patent or utility model
GR01 Patent grant
CU01 Correction of utility model patent

Correction item: Second patentee

Correct: Yang Quzhong

Number: 17

Page: The title page

Volume: 28

CU03 Correction of utility model patent gazette

Correction item: Second patentee

Correct: Yang Quzhong

Number: 17

Volume: 28

ERR Gazette correction

Free format text: CORRECT: 2ND PATENTEE; FROM: NONE TO: YANG QUZHONG

CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120425

Termination date: 20170831

CF01 Termination of patent right due to non-payment of annual fee