CN201306153Y - Crude oil heating heat exchanger - Google Patents

Crude oil heating heat exchanger Download PDF

Info

Publication number
CN201306153Y
CN201306153Y CNU2008202288333U CN200820228833U CN201306153Y CN 201306153 Y CN201306153 Y CN 201306153Y CN U2008202288333 U CNU2008202288333 U CN U2008202288333U CN 200820228833 U CN200820228833 U CN 200820228833U CN 201306153 Y CN201306153 Y CN 201306153Y
Authority
CN
China
Prior art keywords
heat exchanger
heat
heat interchanger
crude oil
communicated
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
CNU2008202288333U
Other languages
Chinese (zh)
Inventor
任长海
任锋
杨在川
白友
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CNU2008202288333U priority Critical patent/CN201306153Y/en
Application granted granted Critical
Publication of CN201306153Y publication Critical patent/CN201306153Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Abstract

The utility model relates to a heat exchanger, in particular to a crude oil heating heat exchanger. The crude oil heating heat exchanger comprises a heat exchanger, and a medium heating furnace for supplying heat energy to the heat exchanger. The heat exchanger adopts a cavity tank; at least nine heat exchange tubes which are bent back and forth from the front part to the rear part are welded on the inner wall of the cavity tank; and the both ends of the heat exchange tubes extend out of the heat exchanger and are respectively communicated with an oil inlet tube and an oil outlet tube. The medium heating furnace adopts a cavity body provided with a water jacket layer; a smoke tube penetrates the center of the medium heating furnace; a natural gas nozzle is installed at the lower part of the smoke tube; and a temperature controller is installed at the rear part of the smoke tube and is communicated with a natural gas inlet tube. A medium gas tube is communicated between the heat exchanger and the medium heating furnace, and a temperature sensor is installed on the outer wall of the heat exchanger which is closely attached to the heat exchange tube and is connected with the circuit of the temperature controller. The crude oil heating heat exchanger has the advantages that the structure is simple, the weight is light, ZGM composite chemical mediator is adopted to replace water to transfer heat, the heat transfer effect is better, the heating temperature can be automatically adjusted according to the crude oil transmission quantity during the process of the crude oil transmission, and the energy source is saved.

Description

The heating crude oil heat interchanger
1, technical field:
The utility model relates to a kind of heat interchanger, relates in particular to a kind of heating crude oil heat interchanger.
2, background technology:
In the manufacturing process of recovering the oil, owing to contain materials such as pitch, mineral tallow in the crude oil, these materials can solidify under normal temperature or low temperature, are unfavorable for the conveying of crude oil.For guaranteeing the conveying of crude oil, need crude oil is heated, make crude oil remain liquid condition.Generally be to adopt water jacket furnace now to heating crude oil, such as: fire tube examination heating water jacket stove, U type water jacket furnace or the like, they all are to rely on to increase area of dissipation, be achieved the purpose of interchange of heat, and be heat transfer medium with water, but the ratio enthalpy of water is low, and heat-transfer effect is undesirable, and saturation water specific enthalpy in the time of 99 ℃ is that 417kj/kg is 504.7kj/kg than enthalpy in the time of 120 ℃.For increasing heat output, just adopt the way that increases heat capacity, the increase equipment of trying one's best increases heat capacity and adorns water more, and general water jacket furnace need add 14 tons water, need absorb a large amount of heats when these water are heated to operating temperature, certainly will cause waste.Simultaneously, it is big to make a water jacket furnace consumptive material, and simultaneously in the course of the work, the natural gas of burning is along with the flow of crude oil is different uncontrollable, and the design maximum stream flow according to crude oil heats always, causes a large amount of waste of natural gas.
3, summary of the invention:
The purpose of this utility model is to propose a kind of simple in structure, and cost of manufacture is low, Controllable Temperature, the heating crude oil heat interchanger of energy conservation.
The purpose of this utility model is achieved in that the heating crude oil heat interchanger, comprises heat interchanger, and the medium heating furnace of heat energy is provided for heat interchanger.Heat interchanger is a cavity jar, be welded with on the inwall at an upper portion thereof at least nine roads from front to back, crooked heat exchanger tube back and forth, heat interchanger is stretched out at the heat exchanger tube two ends, is communicated with oil inlet pipe, flowline respectively.Medium heating furnace is the cavity body that is provided with water jacket layer, and its center is installed with smoke pipe, and smoke pipe bottom installing natural gas nozzle is installed temperature controller thereafter, and and natural gas air inlet pipe conducting.Be communicated with the medium steam pipe between heat interchanger and medium heating furnace, be close to installing one temperature pick up on the heat exchanger tube outer wall at heat interchanger, it is connected with the temperature controller circuit.
The utility model is simple in structure, in light weight, adopt ZGM composite chemical medium place of water to conduct heat, heat-transfer effect is better, in the crude oil transmission course, the based on crude transmission quantity is regulated heating-up temperature, energy conservation automatically, save the cost of manufacture of heat transmitter simultaneously, safety factor height, but the high-temperature gas that natural gas produces second use also, economic environmental protection.
4, description of drawings:
Concrete structure of the present utility model is provided by following drawings and Examples:
Fig. 1 is a heating crude oil heat converter structure schematic diagram.
Legend: 1, thermometer, 2, pressure meter, 3, electromagnetic valve, 4, heat exchanger tube, 5, flowline, 6, chimney, 7, smoke pipe, 8, pedestal, 9, leg, 10, temperature pick up, 11, the medium steam pipe, 12, temperature controller, 13, natural gas nozzle, 14, medium heating furnace, 15, oil inlet pipe, 16, heat interchanger, 17, detector tube.
5, the specific embodiment:
The utility model is not subjected to the restriction of following embodiment, can determine concrete embodiment according to the technical solution of the utility model and actual conditions.
Embodiment: as shown in Figure 1, the heating crude oil heat interchanger comprises heat interchanger 16, and the medium heating furnace 14 of heat energy is provided for heat interchanger 16.Heat interchanger 16 is whole laterally, inclined seat is on pedestal 8, supported by leg 9, it is a cavity jar, be welded with on the inwall at an upper portion thereof at least nine roads from front to back, crooked heat exchanger tube 4 back and forth, heat interchanger 16 is stretched out at heat exchanger tube 4 two ends, is communicated with oil inlet pipe 15, flowline 5 respectively.Medium heating furnace 14 is for being provided with the cavity body of water jacket layer, and its center is installed with smoke pipe 7, and smoke pipe 7 bottoms installing natural gas nozzle 13 is installed temperature controller 12 thereafter, and and natural gas air inlet pipe conducting.Smoke pipe 7 penetrates in the heat interchanger 16, and is divided into three roads, heat interchanger 16 in addition end to converge be a pipe again, and pass heat interchanger 16 and the chimney 6 that is erected on the pedestal 8 is communicated with.Be communicated with medium steam pipe 11 between heat interchanger 16 and medium heating furnace 14, heated medium is managed 11 thus and is fed heat interchanger 16.Be close to installing one temperature pick up 10 on heat exchanger tube 4 outer walls at heat interchanger 16, it is connected with temperature controller 12 circuit.Also be communicated with U-shaped detector tube 17 in heat interchanger 16 upper ends, be equiped with thermometer 1, pressure meter 2 and electromagnetic valve 3 on it side by side.
During use, by the ZGM composite chemical medium in the heat heat medium heating furnace 14 of natural gas burning generation, because heat interchanger 16 is for being in tilted layout, and heat conductivility according to liquid, heated MEDIA FLOW heat exchanger 16 tops, the medium that temperature is low flows back in the water jacket layer of medium heating furnace 14, continues to be heated, thermal medium remains at around the heat exchanger tube 4, strengthens the efficient of the heating crude oil in the exchange heat pipe 4.Collection by heat exchanger tube 4 ambient temperatures in 10 pairs of jars of temperature pick up, changing data signal into sends out and temperature controller 12, temperature controller 12 is regulated the natural gas flow automatically according to setting program, oil flow is big in the heat exchanger tube 4, then heat exchanger tube 4 temperature are corresponding lower, regulate the natural gas flow this moment and increase, it is big that flame becomes; Oil flow is little in the heat exchanger tube 4, and then heat exchanger tube 4 temperature are corresponding higher, and regulate the natural gas flow and reduce this moment, and flame diminishes, thereby changes the medium temperature in the medium heating furnace 14, to reach the purpose that changes Controllable Temperature in the heat interchanger 16.Monitor the parameters in the heat interchanger 16 in real time by the thermometer on the detector tube 17 1, pressure meter 2, if pressure is excessive, open electromagnetic valve 3, release pressure guarantees safety.
Above technical characterictic has constituted most preferred embodiment of the present utility model, and it has stronger compliance and best implementation result, can increase and decrease inessential technical characterictic according to actual needs, satisfies the needs of different situations.

Claims (4)

1, a kind of heating crude oil heat interchanger, comprise heat interchanger, the medium heating furnace of heat energy is provided for heat interchanger, it is characterized in that: heat interchanger is a cavity jar, be welded with at least nine roads on the inwall from front to back at an upper portion thereof, Wan Qu heat exchanger tube back and forth, heat interchanger is stretched out at the heat exchanger tube two ends, respectively and oil inlet pipe, flowline is communicated with, medium heating furnace is the cavity body that is provided with water jacket layer, its center is installed with smoke pipe, smoke pipe bottom installing natural gas nozzle, install temperature controller thereafter, and and the conducting of natural gas air inlet pipe, between heat interchanger and medium heating furnace, be communicated with the medium steam pipe, be close to installing one temperature pick up on the heat exchanger tube outer wall at heat interchanger, it is connected with the temperature controller circuit.
2, heating crude oil heat interchanger as claimed in claim 1 is characterized in that: also be communicated with the U-shaped detector tube in the heat interchanger upper end, be equiped with thermometer, pressure meter and electromagnetic valve on it side by side.
3, heating crude oil heat interchanger as claimed in claim 1, it is characterized in that: smoke pipe penetrates in the heat interchanger, and is divided into three roads, heat interchanger in addition end to converge be a pipe again, and pass heat interchanger and the chimney that is erected on the pedestal is communicated with.
4, heating crude oil heat interchanger as claimed in claim 1 is characterized in that: heat interchanger is whole laterally, inclined seat on pedestal, support by leg.
CNU2008202288333U 2008-12-08 2008-12-08 Crude oil heating heat exchanger Expired - Fee Related CN201306153Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2008202288333U CN201306153Y (en) 2008-12-08 2008-12-08 Crude oil heating heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2008202288333U CN201306153Y (en) 2008-12-08 2008-12-08 Crude oil heating heat exchanger

Publications (1)

Publication Number Publication Date
CN201306153Y true CN201306153Y (en) 2009-09-09

Family

ID=41098620

Family Applications (1)

Application Number Title Priority Date Filing Date
CNU2008202288333U Expired - Fee Related CN201306153Y (en) 2008-12-08 2008-12-08 Crude oil heating heat exchanger

Country Status (1)

Country Link
CN (1) CN201306153Y (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108702812A (en) * 2016-02-18 2018-10-23 韦巴斯托股份公司 Heat exchanger system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108702812A (en) * 2016-02-18 2018-10-23 韦巴斯托股份公司 Heat exchanger system
CN108702812B (en) * 2016-02-18 2022-06-21 韦巴斯托股份公司 Heat exchanger system

Similar Documents

Publication Publication Date Title
CN202141195U (en) Vacuum hot water boiler with waste heat recycling device
CN104296542B (en) Heat-energy recovery system of high-temperature material and method of work thereof
CN102563867A (en) Solar-heating assisted salt melting system
CN101956969A (en) Fused salt coil tube type steam generation method and device
CN109405288B (en) Heating furnace flue gas waste heat recovery device for oil field
CN202470425U (en) Molten salt system
CN201306153Y (en) Crude oil heating heat exchanger
CN202885295U (en) Intelligent solar water heater circulating system
CN209197545U (en) Solid heat reservoir with superheated steam heat-exchanger rig
CN103408008B (en) A kind of activation furnace
CN205011383U (en) System for natural gas partial oxidation system synthetic gas waste heat recovery
CN204625576U (en) A kind of Novel water cooling wall for coal gasifier
CN101266075B (en) Cylinder type gas heating stove improvement structure
CN201487925U (en) Multifunctional steam generating furnace
CN202057033U (en) Energy-saving steam water boiler
CN101261037A (en) Cylinder type gas heating stove heat flow field improvement structure
CN202792886U (en) Energy-saving baking system
CN205767349U (en) A kind of die temperature control device
CN205372644U (en) Heating waste heat collection device
CN219474347U (en) High-efficiency waste heat recovery device for coal-electricity enterprises
CN203190393U (en) Heating boiler
CN201203266Y (en) Rotating cylinder type gas heating furnace
CN202181286U (en) Fused salt heat exchange system for gas making furnace jacket
CN203586171U (en) Low temperature difference organic working medium evaporator utilizing low temperature heat energy
CN213686761U (en) Split pressure-bearing preheating type steam generator

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20090909

Termination date: 20111208