CN105056551A - Novel cooling steam supply equipment - Google Patents
Novel cooling steam supply equipment Download PDFInfo
- Publication number
- CN105056551A CN105056551A CN201510471298.9A CN201510471298A CN105056551A CN 105056551 A CN105056551 A CN 105056551A CN 201510471298 A CN201510471298 A CN 201510471298A CN 105056551 A CN105056551 A CN 105056551A
- Authority
- CN
- China
- Prior art keywords
- cooling
- cooling tower
- pipe
- steam boiler
- steam
- 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.)
- Pending
Links
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The present invention discloses novel cooling steam supply equipment, including a cooling tower and a steam boiler. The cooling tower contains a snakelike cooling pipe; the cooling tower contains a recovery gas pipe and a liquid recovery cabin; the steam boiler is provided with a water inlet pipe and a water outlet pipe; and the water outlet of the snakelike cooling pipe of the cooling tower is connected to the water inlet pipe of the steam boiler through an insulation pipe. The equipment not only combines many functions in one, but also saves energy, improves work efficiency and quality and reduces plant costs. The equipment has better economic value and market competitiveness.
Description
Technical field
The invention belongs to technical field of mechanical equipment, particularly relate to a kind of novel cooling steam supply equipment.
Background technology
The step that Oils and fats enterprise produces oil is as follows: first oil plant is formed after pretreatment material embryo or pre-pressed cake, then solvent naphtha and its mixing are put into leaching equipment, liquid miscella and solid residue is obtained after extraction extraction, residue filter is obtained miscella, then obtains pure oil after gaseous state separation is carried out to miscella.The necessary technological process being separated and being not only and producing branded oil of vaporizing is carried out to solvent naphtha, but also can recycle, reduce costs.The leaching workshop of the traditional forms of enterprises uses oil cooling but tower when vaporizing recovered solvent oil, and method is that tap water at normal temperature is injected cooling tower, carries out heat exchange with gaseous solvent oil, recycles again pumping in cooling tower after outdoor cooling.The annual normal temperature of running water is 15 DEG C, and the temperature after oily cooling tower is 45 DEG C, though afterwards through outdoor cooling, temperature is always high than mean temperature, and the effect again utilized reduces.
Steam boiler is the equipment of steam of tap water at normal temperature being vaporized with coal-fired heat to obtain, and the industrial production in factory and employee live and mostly be unable to do without steam boiler, and made steam can directly for it provides power or heat energy.
Summary of the invention
The invention provides a kind of novel cooling steam supply equipment, can be used for, in the daily productive life of Oils and fats enterprise, having energy-saving and cost-reducing, reduce the feature of production cost.
A kind of novel cooling steam supply equipment, comprises and being made up of cooling tower and steam boiler, containing spiral coil cooling tube in described cooling tower; Containing reclaiming tracheae and liquids recovery storehouse in described cooling tower; Described steam boiler is provided with water inlet pipe and steam outlet pipe; The spiral coil cooling tube delivery port of described cooling tower is connected with the water inlet pipe of steam boiler by utilidor.
Further, described utilidor is polyurethane foamed thermal-insulating pipeline.
The present invention has following beneficial effect: the annual normal temperature of running water is 15 DEG C, temperature after oily cooling tower is 45 DEG C, the temperature flowing into steam boiler oral siphon through utilidor is 40 ~ 45 DEG C, therefore can reduce steam boiler by water from normal temperature burning to the coal consumption of 40 ~ 45 DEG C; And oily cooling tower is only with tap water at normal temperature cooling, chilling temperature is low and constant, has good cooling effect, and the spiral coil cooling tube be furnished with in addition increases contact area, improves operating efficiency, and the rate of recovery of solvent naphtha is increased.This equipment not only gathers multi-function in integral whole, and can save energy reduction of discharging, increases work efficiency and quality, reduces plant produced cost, has good economic worth and the market competitiveness.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
Detailed description of the invention
Embodiment 1
In order to further describe the present invention, Fig. 1 please be participate in.
A kind of novel cooling steam supply equipment, comprises and being made up of cooling tower 1 and steam boiler 10, containing spiral coil cooling tube 2 in described cooling tower 1; Containing reclaiming tracheae 3 and liquids recovery storehouse 5 in described cooling tower 1; Described steam boiler is provided with water inlet pipe 12 and steam outlet pipe 13; Spiral coil cooling tube 2 delivery port of described cooling tower 1 is connected with the water inlet pipe 12 of steam boiler 10 by utilidor 11.
Further, described utilidor 11 is polyurethane foamed thermal-insulating pipeline.
The present embodiment is tested No. 6 solvent naphthas and anthracite, and particular content is as follows:
In the spiral coil cooling tube 2 that tap water at normal temperature is introduced in oily cooling tower 1 through water inlet 101, again gaseous state No. 6 solvent naphthas 4 separated from miscella are passed in the recovery tracheae 3 of oily cooling tower 1, after a period of time, gaseous state No. 6 solvent naphthas 4 can be liquefied as liquid No. 6 solvent naphthas 7 and be collected in liquids recovery storehouse 5, and the tap water at normal temperature after work becomes intensification running water by the delivery port 102 of spiral coil cooling tube 2 and flows out, flow in the water inlet pipe 12 of steam boiler 10 through utilidor 11, again through anthracitic heating, become steam running water and flow out from steam outlet pipe 13.
Comparative example 1
Respectively No. 6 solvent naphthas and anthracite are tested by conventional method.
Following table is the correction data of two embodiments:
| Comparative example 1 | Embodiment 1 | |
| To vaporize one ton of running water anthracite consumption (kilogram) | 118 | 85 |
| No. 6 solvent naphtha consumption rates (kg/tonne) | 5.1 | 5.0 |
Claims (2)
1. a novel cooling steam supply equipment, comprises and being made up of cooling tower and steam boiler, it is characterized in that, containing spiral coil cooling tube in described cooling tower; Containing reclaiming tracheae and liquids recovery storehouse in described cooling tower; Described steam boiler is provided with water inlet pipe and steam outlet pipe; The spiral coil cooling tube delivery port of described cooling tower is connected with the water inlet pipe of steam boiler by utilidor.
2. one according to claim 1 novel cooling steam supply equipment, is characterized in that, described utilidor is polyurethane foamed thermal-insulating pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510471298.9A CN105056551A (en) | 2015-08-05 | 2015-08-05 | Novel cooling steam supply equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510471298.9A CN105056551A (en) | 2015-08-05 | 2015-08-05 | Novel cooling steam supply equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105056551A true CN105056551A (en) | 2015-11-18 |
Family
ID=54486194
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510471298.9A Pending CN105056551A (en) | 2015-08-05 | 2015-08-05 | Novel cooling steam supply equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105056551A (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201050774Y (en) * | 2007-10-26 | 2008-04-23 | 中国石油天然气第八建设有限公司 | Subcritical pressure steam injection boiler |
| CN203384954U (en) * | 2013-06-18 | 2014-01-08 | 广州天孜环保节能科技有限公司 | Waste heat recycling steam boiler |
| JP2014228222A (en) * | 2013-05-24 | 2014-12-08 | 株式会社サムソン | Boiler with water supply preheater |
| CN204005918U (en) * | 2014-06-04 | 2014-12-10 | 惠州九鼎饲料科技有限公司 | Power economized boiler |
| CN104235825A (en) * | 2013-06-13 | 2014-12-24 | 烟台龙源电力技术股份有限公司 | Boiler flue gas waste heat recycling system |
-
2015
- 2015-08-05 CN CN201510471298.9A patent/CN105056551A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201050774Y (en) * | 2007-10-26 | 2008-04-23 | 中国石油天然气第八建设有限公司 | Subcritical pressure steam injection boiler |
| JP2014228222A (en) * | 2013-05-24 | 2014-12-08 | 株式会社サムソン | Boiler with water supply preheater |
| CN104235825A (en) * | 2013-06-13 | 2014-12-24 | 烟台龙源电力技术股份有限公司 | Boiler flue gas waste heat recycling system |
| CN203384954U (en) * | 2013-06-18 | 2014-01-08 | 广州天孜环保节能科技有限公司 | Waste heat recycling steam boiler |
| CN204005918U (en) * | 2014-06-04 | 2014-12-10 | 惠州九鼎饲料科技有限公司 | Power economized boiler |
Non-Patent Citations (1)
| Title |
|---|
| 刘玉兰: "《油脂制取与加工工艺学》", 30 November 2009, 科学出版社 * |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204815724U (en) | Device is optimized to transform technology condensate strip | |
| CN103613126B (en) | A kind of method and system removing vanadium impurity from titanic tetrachloride | |
| CN103933923A (en) | Continuous reaction production line consisting of multiple serially connected reaction kettles | |
| CN103045298A (en) | System for recovering cracking fraction fuel in waste oil | |
| CN103159376A (en) | Negative pressure ammonia steaming process method of using coking circulating ammonia water waste heat to dispose residual ammonia water | |
| CN101445747A (en) | Hydrofining process integration method | |
| CN104787946B (en) | A kind of wholly-owned source utilization process of steel rolling spent acid | |
| CN203065426U (en) | System used for recycling splitting fraction fuel oil from waste oil and atmospheric distillation system | |
| CN103435508B (en) | The preparation technology of N, N-diethylformamide and device thereof | |
| CN210729532U (en) | 1, 5-naphthalene diisocyanate thermal reaction reflux unit | |
| CN105056551A (en) | Novel cooling steam supply equipment | |
| CN202705309U (en) | Waste lubricating oil regeneration and molecular distillation two-section combination device | |
| CN216629750U (en) | System for separate pentaerythritol and calcium formate from pentaerythritol mother liquor | |
| CN104447340B (en) | DOP esterification system and production technique | |
| CN108441251B (en) | Cryogenic distillation process | |
| CN210595940U (en) | Heat conduction oil processing device | |
| CN106947547A (en) | A kind of powdered coal pressuring gasified technique produces the steam self-support method of synthesis ammonia system | |
| CN204111354U (en) | A kind of sour water steam stripping at reduced pressure device | |
| CN109971513B (en) | Multi-stage cooling process and device for coke oven crude gas | |
| CN102876351A (en) | Heating, flashing and separating device | |
| CN103833592A (en) | Material flow heat recovering process and device in acrylonitrile production device | |
| CN203990562U (en) | Many the new type of continuous reaction production lines that reactor is composed in series | |
| CN204787873U (en) | Two pressures are from deoxidization coal gasification waste heat recovery system | |
| CN103361104A (en) | On-line descaling apparatus for steam jet cooler at top of shallow vacuum tower of atmospheric-vacuum distillation unit used for crude oil refining | |
| CN203362451U (en) | Waste heat recovery device and air compressor system with waste heat recovery device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20151118 |