KR200160985Y1 - Heat exchanger for regenerating of waste oil - Google Patents
Heat exchanger for regenerating of waste oil Download PDFInfo
- Publication number
- KR200160985Y1 KR200160985Y1 KR2019970027527U KR19970027527U KR200160985Y1 KR 200160985 Y1 KR200160985 Y1 KR 200160985Y1 KR 2019970027527 U KR2019970027527 U KR 2019970027527U KR 19970027527 U KR19970027527 U KR 19970027527U KR 200160985 Y1 KR200160985 Y1 KR 200160985Y1
- Authority
- KR
- South Korea
- Prior art keywords
- pipe
- waste oil
- heat exchanger
- distribution pipe
- waste
- 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
Links
- 239000002699 waste material Substances 0.000 title claims abstract description 31
- 230000001172 regenerating effect Effects 0.000 title description 2
- 230000008929 regeneration Effects 0.000 claims abstract description 5
- 238000011069 regeneration method Methods 0.000 claims abstract description 5
- 230000006698 induction Effects 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 2
- 230000003252 repetitive effect Effects 0.000 claims 1
- 239000012535 impurity Substances 0.000 abstract description 6
- 239000000203 mixture Substances 0.000 abstract description 4
- 239000002245 particle Substances 0.000 abstract description 4
- 239000003921 oil Substances 0.000 description 24
- 238000000034 method Methods 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 2
- 210000005239 tubule Anatomy 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 238000003260 vortexing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M175/00—Working-up used lubricants to recover useful products ; Cleaning
- C10M175/0025—Working-up used lubricants to recover useful products ; Cleaning by thermal processes
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M175/00—Working-up used lubricants to recover useful products ; Cleaning
- C10M175/0025—Working-up used lubricants to recover useful products ; Cleaning by thermal processes
- C10M175/0033—Working-up used lubricants to recover useful products ; Cleaning by thermal processes using distillation processes; devices therefor
Landscapes
- Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
폐유재생용 열교환기로서 단위시간에 많은 폐유를 통과시키면서 열접족면적을 크게하고 와류를 형성시키는 구조로되어있어 폐유속에 혼입된 불순물 덩어리를 유로부터 쉽게 분리할 수 있게하고 폐유속에 뭉쳐진 혼합물 입자를 파괴하여 개개의 성분으로 분리할 수 있는 기능을 갖는 열교환기As a heat exchanger for waste oil regeneration, it has a structure that increases the thermal contact area and forms vortices while passing a large amount of waste oil in a unit time, making it easy to separate the clumps of impurities entrained in the waste flow from the oil and destroy the mixture particles aggregated in the waste flow. Heat exchanger with the ability to separate into individual components
Description
본 고안은 해상오염류, 선박폐유, 자동차폐유 각종 폐윤활유, 폐기계유 등의 폐유재생공정에서 사용되는 폐유재생용 열교환기에 관한 것이다.The present invention relates to a heat exchanger for waste oil regeneration used in waste oil regeneration processes such as marine pollutants, marine waste oil, automobile waste oil, various waste lubricating oils, waste oils, and the like.
더욱 구체적으로는, 일정온도를 유지할수 있고 단위시간에 다량의 폐유를 통과시킬수 있으며 와류를 형성시킬수 있는 열매체 수장조와 열매체를 통과하는 열교환관으로 구성된 폐유재생용 열교환기를 제공함에 있다.More specifically, the present invention provides a heat exchanger for waste oil regeneration comprising a heat medium tank capable of maintaining a constant temperature, passing a large amount of waste oil in a unit time, and forming a vortex and a heat exchange tube passing through the heat medium.
폐유를 재생하는 공정중에 사용되는 하나의 장치 분야로서 종래 열교환관을 설치하여 구성된 열교환기는 정상류의 연속적인 흐름으로 단순히 열교환에만 그치는 열교환기로서 본고안에서와 같이 단위시간에 폐유의 통과하는 양을 많게하고 와류를 형성시키므로서 기름에 부착된 불순물을 분리하는 기능을 갖지 못한다.As a field of equipment used in the process of regenerating waste oil, a heat exchanger constructed by installing a conventional heat exchanger tube is a heat exchanger which is merely a heat exchanger in a continuous flow of steady flow, and increases the amount of waste oil passed in a unit time as in this paper. It does not have the function of separating impurities attached to oil by forming vortices.
폐유에 혼입되어 있는 고형 또는 반고형의 불순물은 기름으로부터 쉽게 분리제거할수 있도록함에 목적이 있고, 본고안에 있어서도 열매체를 통과시키므로서 폐유온도를 상승시켜 점도를 떨어뜨리므로서 점성을 약화시켜 불순물을 쉽게 분리할수 있게하고, 혼합물로 뭉쳐진 입자들을 와류 형성시키므로서 와해되어 개개의 성분으로 분리될수 있게 하고, 다음 공정에서 불순물이 슬러지로 침강 제거되거나 부상되어 분리제거되게 하는 구조의 장치를 얻고져 함에 있다.Solid or semi-solid impurities mixed into the waste oil are intended to be easily separated and removed from the oil.In this paper, too, the heat is passed through the heat medium and the waste oil temperature is increased to decrease the viscosity while decreasing the viscosity, thereby making it easier to remove the impurities. It is possible to obtain a device having a structure that allows separation, disintegrates and separates into individual components by vortexing particles that are aggregated into a mixture, and in the following process, impurities are sedimented or flocculated by sludge or floated.
제1a도는 본 고안의 측단면도.Figure 1a is a side cross-sectional view of the present invention.
제1b도는 본 고안의 요부 발췌사시도.Figure 1b is a perspective view of the main portion of the present invention.
본고안은 폐유를 가열하므로서 점성을 떨어뜨려 폐유속에 혼입된 고형 및 반고형 불순물을 기름으로부터 분리하고 기름, 각종혼합물로 뭉쳐진 입자를 와해하여 개개의 성분으로 분리하므로서 폐유재생을 효율적으로 수행하는 폐유재생 공정중에 사용되는 하나의 장치로서 이를 구체적으로 설명하면 제1a도에서와 같이 정부 일측에 설치된 열매체 구입구(1)와 하부일측에 설치된 열매체 배출구(2)를 갖는 열매체 수장조(3)와 이 수장조의 외부 하측에 있는 스팀주입구(4)로부터 유도되는 스팀관(5)이 수장조 내측 하부에 환상형태로 배치되면서 스팀관(5) 하단이 스팀 배출구(6)에 연결되어 있고 수장조(3)의 측면 윗쪽에 있는 폐유 주입구(7)로부터 유입된 유도관(8)이 제1분배관(9)의 일측에 연통되고 제1분배관(9)으로부터 여러개의 세관(9')들이 분기되어 제2분배관(10)에 연결되며 제2분배관(10)으로부터 다시 세관(10')들이 연결되어 제3분배관(11)에 연결되고 제3분배관으로부터 세관(11')들이 제4분배관(12)으로 연결되는 동일 반복형태로 구성되어 최종분배관(13)의 일측으로부터 유도관(14)에 유도되어 폐유 배출구(15)로 연결된 구조이다.This paper reduces waste viscosity by heating waste oil and separates solid and semi-solid impurities contained in the waste flow from the oil, and disintegrates the particles aggregated into oil and various mixtures into separate components to efficiently recycle waste oil. As a device used in the process, it will be described in detail as shown in Fig. 1a and the heat medium storage tank 3 and the heat medium having a heat medium purchase port (1) installed on one side of the government and a heat medium outlet (2) installed on the lower one side. The steam pipe (5) guided from the steam inlet (4) in the outer lower side of the tank is arranged in an annular shape on the inner bottom of the storage tank, the bottom of the steam pipe (5) is connected to the steam outlet (6) and the storage tank (3) The induction pipe (8) introduced from the waste oil inlet (7) on the side of the upper side is in communication with one side of the first distribution pipe (9), and several tubules (9 ') branched from the first distribution pipe (9) 2 It is connected to the pipe 10 and the second tubular pipe 10 is connected to the tubules 10 'again connected to the third branch pipe (11) and the third pipe (11') from the third branch pipe (4) 12) is configured in the same repeating form is connected to the induction pipe 14 from one side of the final distribution pipe 13 is a structure connected to the waste oil outlet (15).
본고안에서 폐유 가열수단이 열매체로 되어 있어 열의 손실을 줄일수 있고 일정온도를 유지할수 있는 잇점이 있으며 제1b도에서와 같이 열교환관은 폐유주입구(7)로부터 유입된 유도관(8)의 폐유는 제1분배관(9)에 정면으로 충돌하게 되고 제1분배관(9)으로부터 분기된 세관(9')으로 흘러들어 가는 폐유는 다시 제2분배관(10)을 형성하는 관면에 정면으로 출동하는 흐름으로 와류를 생성시키므로서 온도상승으로 점성이 떨어진 폐유의 혼입된 뭉쳐진 입자들을 파괴하면서 개개의 성분으로 분리되어 혼합물의 제거효율을 높일 수 있고 다수로 분기된 세관으로 단위시간에 폐유통과량을 크게 하면서도 열접촉면적을 크게하여 열효율을 높일수 있는 구조로된 열교환기라 할수 있다.In this paper, the waste oil heating means is made of heat medium, which can reduce heat loss and maintain a constant temperature. As shown in FIG. 1B, the heat exchanger tube has the waste oil of the induction tube 8 introduced from the waste oil inlet 7 The waste oil which collides with the first distribution pipe 9 in front and flows into the branch pipe 9 'branched from the first distribution pipe 9 again flows out to the pipe surface forming the second distribution pipe 10 again. The vortices are generated by the flow of air, which breaks down the aggregated particles of the waste oil that have become less viscous due to the temperature rise, and is separated into individual components, thereby improving the removal efficiency of the mixture. It is a heat exchanger with a structure that can increase the thermal efficiency while increasing the thermal contact area.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR2019970027527U KR200160985Y1 (en) | 1997-10-02 | 1997-10-02 | Heat exchanger for regenerating of waste oil |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR2019970027527U KR200160985Y1 (en) | 1997-10-02 | 1997-10-02 | Heat exchanger for regenerating of waste oil |
Publications (2)
Publication Number | Publication Date |
---|---|
KR980002902U KR980002902U (en) | 1998-03-30 |
KR200160985Y1 true KR200160985Y1 (en) | 1999-11-15 |
Family
ID=19511311
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR2019970027527U Expired - Fee Related KR200160985Y1 (en) | 1997-10-02 | 1997-10-02 | Heat exchanger for regenerating of waste oil |
Country Status (1)
Country | Link |
---|---|
KR (1) | KR200160985Y1 (en) |
-
1997
- 1997-10-02 KR KR2019970027527U patent/KR200160985Y1/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
KR980002902U (en) | 1998-03-30 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4655914A (en) | Method and apparatus for filtering impurities out of fluid | |
GB2220374A (en) | "a liquid separator" | |
JPH0554365B2 (en) | ||
US3977850A (en) | Centrifugal separator | |
GB1165128A (en) | Gravity Separation of Immiscible Liquids | |
US4213865A (en) | Apparatus for separating sludge, oil and the like from contaminated water | |
US4276059A (en) | Deaerator for pulp stock | |
US5143611A (en) | Apparatus for separating oil from water | |
KR200160985Y1 (en) | Heat exchanger for regenerating of waste oil | |
GB2067919A (en) | Apparatus for venting and dearating a liquid circuit | |
EP1697262A1 (en) | Flotation separator | |
US4662908A (en) | Device for removing bubbles from liquid | |
RU2190450C2 (en) | Gas-and-liquid separator | |
GB9812654D0 (en) | Improvements in or relating to separators | |
US4612120A (en) | Axisymmetrical separator for separating solids and gas from a fluid medium | |
US4544483A (en) | Dynamic, reverse-flow oil purifier device | |
KR100244945B1 (en) | Moisture Separation Device for Automotive Diesel Oil | |
GB2035118A (en) | Separation of immiscible liquids | |
RU2114679C1 (en) | Self-cleaning filter | |
RU2227791C1 (en) | Device for cleaning oily waste water | |
WO1999043439A1 (en) | Device and method for the separation of fluids | |
SU772598A2 (en) | Combination-type hydraulic cyclone | |
SU997823A2 (en) | Hydraulic cyclone | |
SU544445A1 (en) | Apparatus for separating and degassing a liquid | |
CN217092189U (en) | Small-size vertical coalescence divides oil machine |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A201 | Request for examination | ||
G15R | Request for early publication | ||
UA0108 | Application for utility model registration |
Comment text: Application for Utility Model Registration Patent event code: UA01011R08D Patent event date: 19971002 |
|
UA0201 | Request for examination |
Patent event date: 19971002 Patent event code: UA02012R01D Comment text: Request for Examination of Application |
|
UG1501 | Laying open of application |
Comment text: Request for Laying-Open of Early Application Patent event code: UG15011R01I Patent event date: 19971002 |
|
E902 | Notification of reason for refusal | ||
UE0902 | Notice of grounds for rejection |
Comment text: Notification of reason for refusal Patent event code: UE09021S01D Patent event date: 19990525 |
|
E701 | Decision to grant or registration of patent right | ||
UE0701 | Decision of registration |
Patent event date: 19990805 Comment text: Decision to Grant Registration Patent event code: UE07011S01D |
|
REGI | Registration of establishment | ||
UR0701 | Registration of establishment |
Patent event date: 19990824 Patent event code: UR07011E01D Comment text: Registration of Establishment |
|
UR1002 | Payment of registration fee |
Start annual number: 1 End annual number: 3 Payment date: 19990825 |
|
UG1601 | Publication of registration | ||
UR1001 | Payment of annual fee |
Payment date: 20020820 Start annual number: 4 End annual number: 4 |
|
UR1001 | Payment of annual fee |
Payment date: 20030825 Start annual number: 5 End annual number: 5 |
|
UR1001 | Payment of annual fee |
Payment date: 20040825 Start annual number: 6 End annual number: 6 |
|
UR1001 | Payment of annual fee |
Payment date: 20050825 Start annual number: 7 End annual number: 7 |
|
UR1001 | Payment of annual fee |
Payment date: 20060825 Start annual number: 8 End annual number: 8 |
|
UR1001 | Payment of annual fee |
Payment date: 20070817 Start annual number: 9 End annual number: 9 |
|
FPAY | Annual fee payment |
Payment date: 20080825 Year of fee payment: 10 |
|
UR1001 | Payment of annual fee |
Payment date: 20080825 Start annual number: 10 End annual number: 10 |
|
LAPS | Lapse due to unpaid annual fee | ||
UC1903 | Unpaid annual fee |
Termination date: 20100710 Termination category: Default of registration fee |