CN206310528U - Light hydrocarbon system for providing cleaning cloth grass steam - Google Patents
Light hydrocarbon system for providing cleaning cloth grass steam Download PDFInfo
- Publication number
- CN206310528U CN206310528U CN201621348276.XU CN201621348276U CN206310528U CN 206310528 U CN206310528 U CN 206310528U CN 201621348276 U CN201621348276 U CN 201621348276U CN 206310528 U CN206310528 U CN 206310528U
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- tank
- gas tank
- light hydrocarbon
- air
- processed
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Abstract
The utility model discloses a kind of light hydrocarbon system for providing cleaning cloth grass steam, including gas tank processed, oil tank, enter gas tank, hydronic heater, neutralizing tank and gas tank.The oil tank of liquid light hydrocarbon of being stored with connects gas tank processed to its input liquid light hydrocarbon by pipeline.Enter gas tank and the forced air that gas tank processed is input into promotion light hydrocarbon to it is connected by pipeline.Hydronic heater is connected by pipeline and gas tank processed is heated.Gasified lighter hydrocarbons into high concentration by being input into liquid light hydrocarbon mixing forced air physical transformations in the presence of high temperature in gas tank processed, and connected by pipeline high concentration gasifies lighter hydrocarbons output a to neutralizing tank.The mixed air-conditioning pressure device of neutralizing tank connection one, the mixed air-conditioning pressure device causes that the gasification lighter hydrocarbons of air mixture and the composition ratio of air are 15 21 in neutralizing tank by input air in neutralizing tank:85‑79.Air mixture in neutralizing tank connects gas tank and is stored by pipeline.
Description
Technical field:
The utility model is related to energy environment protection technical field, more particularly to a kind of for providing the light of cleaning cloth grass steam
Hydrocarbon gasification system.
Background technology:
In recent years, with China's rapid economic development, energy-output ratio is growing day by day, although the annual a large amount of import stones of China
Oil and gas, but the pressure of energy scarcity becomes increasingly conspicuous.At the same time, liquid light hydrocarbon was produced as oil gas field and oil plant
Derivative in journey, is that a kind of oil gas fields most of at home and abroad, gas field, oil plant, petrochemical plant can see pentane
This association accessory substance of hydrocarbon mixture.Due to the dispersion of its place of production, store up the reasons such as high cost, complicated components.Liquid light hydrocarbon is difficult to add
Efficiently to utilize.So far, the economic use of main flow never worldwide is found, is considered as that " that abandons can in the industry
Cherish, food it is dull " " chicken ribs " resource, form oil field and refinery factory overhead visible " torch " combustion phenomena throughout the year, both wave
Expense resource pollutes environment again.
However, liquid light hydrocarbon but shoulds be regarded as a different matter by the light-hydrocarbon gas formed after gasification process.Light-hydrocarbon gas conduct
A kind of efficient, cleaning, the high quality gas fuel of low cost, have common ancestry homologous with natural gas, liquefied petroleum gas, are described as " green by people
Color fuel ".It is significant to improving China's energy consumption structure, raising efficiency of energy utilization.
Currently, fuel price remains high, and is especially generally gone up with industrial fuels such as coal gas, natural gases, and this is to relying on
The cloth grass washing industry of combustion gas is a heavy cost burden, seriously hinders the sustainable development of these enterprises.It is this lighter hydrocarbons
Combustion gas increasingly receives the concern and welcome of these enterprises with its cheap economy.
Utility model content:
In view of above-mentioned technical problem, the utility model is there is provided a kind of light hydrocarbon for providing cleaning cloth grass steam
System.The system equipment with byproduct C5, the C6 in oil, natural gas extraction and process be gas raw material processed, by efficient
The physical vapor mode of safety, is converted into gaseous mixed combustible gas body, then be pipelined to end by normal pressure liquid light hydrocarbon
End subscriber.
Concrete technical scheme of the present utility model is as follows:
Light hydrocarbon system for providing cleaning cloth grass steam, including gas tank processed, oil tank, enter gas tank, liquid and follow
Ring heater, neutralizing tank and gas tank;Characterized in that, the oil tank of the liquid light hydrocarbon that is stored with connects gas processed by pipeline
Tank is input into liquid light hydrocarbon to it;It is described enter gas tank gas tank processed is connected by pipeline the pressurization sky for promoting light hydrocarbon is input into it
Gas;The hydronic heater is connected come to its lasting liquid of the input with heat energy by building circulation line with gas tank processed
Then realize heating gas pot liquid processed;By being input into liquid light hydrocarbon in mixing forced air and height in the gas tank processed
Physical transformations are into high concentration gasification lighter hydrocarbons in the presence of temperature, and connected high concentration gasification lighter hydrocarbons output a to neutralization by pipeline
Tank;The mixed air-conditioning pressure device of the neutralizing tank connection one, the mixed air-conditioning pressure device causes neutralization by input air in neutralizing tank
The gasification lighter hydrocarbons of in-tank mixing combustion gas are 15-21 with the component ratio of air:85-79;Air mixture in the neutralizing tank is led to
Cross pipeline connection gas tank and stored.It is final that by gas tank, pressure regulation exports and carries out burning to boiler and produce cleaning cloth grass institute again
The steam of needs.
In such scheme, the oil tank is provided with filtering and pressue device.
In such scheme, the oil tank is connected with some for the blow-down pipe to oil tank exhaust step-down.So with
Just ensure that liquid light hydrocarbon efficiently, smoothly injects empty oil tank from oil truck.
In such scheme, it is described enter gas tank by one end connect air compressor come to gas tank processed input forced air.
In such scheme, the hydronic heater includes being connected liquid circulation line, water tank and heating with gas tank processed
Source, the heating source is to connect electric heater or the outside steam that access water tank is connected by pipeline that water tank is heated to it
Source.
In such scheme, the liquid circulation line connection is placed in the liquid coil pipe in gas tank processed.
In such scheme, the pressure of air mixture is dropped to 5- by the gas tank by connecting a dropping valve from 15-30kpa
13kpa, and by pipeline final output to burning boiler.
In such scheme, described mixed air-conditioning pressure device one end is connected with gas tank is entered, and other end connection neutralizing tank is used to adjust
The gaseous state lighter hydrocarbons of air mixture and the composition ratio of air.
The beneficial effects of the utility model are as follows:
1. whole equipment utilizes natural temperature gas, and low pressure gas, minute-pressure are used, and are not added with any additive, combustion adjuvant etc.
Chemical raw material, rate of gasification 100%, without raffinate, without Hui Ning, supplies stabilization throughout the year.
2. atmospheric pressure processed and discharge pressure are only 0.13-0.35 kilograms to whole equipment in the process of running, the pressure of liquefied gas
Power is 6-8 kilograms, and the pressure of coal gas is 3-4 kilograms, and the pressure of natural gas is 3.2 kilograms, and gaseous-pressure more high risk is more
Greatly, gaseous-pressure is more low safer.
3. the lighter hydrocarbons for being gasified using the equipment, its combustion heat value be up to 10800 kilocalories/kilogram, and in the past natural gas
Combustion heat value for 7500 ~ 8500 kilocalories/kilogram, for traditional cloth grass cleaning enterprise, not only raw material turns gasification lighter hydrocarbons
Change is with low cost, and combustion heat value also exceeds conventional natural gas, and to its day-to-day operations cloth grass steaming, drying, plating needs greatly
For amount fuel combustion, the equipment is an extraordinary energy-saving emission-reducing apparatus.With great economy and the feature of environmental protection.
4. placement area need not additionally be taken for cloth grass washing enterprise using the equipment, therefore promote not by field
Ground limitation, addressing is more flexible.
Brief description of the drawings:
The utility model is further illustrated below in conjunction with the drawings and specific embodiments.
Fig. 1 is light hydrocarbon overall system architecture figure described in the utility model.
Fig. 2 is the specific knot of the hydronic heater being connected with gas tank processed in light hydrocarbon system described in the utility model
Structure block diagram.
Specific embodiment:
In order that technological means, creation characteristic, reached purpose and effect that the utility model is realized are easy to understand, under
Face combines and is specifically illustrating, and the utility model is expanded on further.
As depicted in figs. 1 and 2, the light hydrocarbon system for providing cleaning cloth grass steam described in the utility model,
It includes gas tank processed 10, oil tank 20, enters gas tank 30, hydronic heater 40, neutralizing tank 50 and gas tank 60.
Wherein, the oil tank 20 of liquid light hydrocarbon of being stored with connects gas tank 10 processed to its input liquid light hydrocarbon by pipeline.Storage
Oil tank 20 is provided with filtering and pressue device(Not shown in figure).And some are connected with for being put to oil tank exhaust step-down
Blank pipe 21.So efficiently, smoothly empty oil tank is injected to ensure liquid light hydrocarbon from oil truck.
Enter gas tank 30 and the forced air that gas tank 10 processed is input into promotion light hydrocarbon to it is connected by pipeline.Specifically,
It is to connect air compressor 31 by one end to be input into forced air to gas tank processed 10 to enter gas tank 30.
Hydronic heater 40 carries heat energy by being connected with the structure circulation line of gas tank processed 10 to its lasting input
Liquid then realize heating gas tank processed.Specifically, hydronic heater 40 includes being connected liquid with gas tank processed
Circulation line 42, water tank 44 and heating source.Liquid circulation line 42 connects the liquid coil pipe 11 being placed in gas tank processed.This sample liquid
Body circulation heater 40 injects the liquid with high temperature by liquid circulation line 42 to gas tank processed 10(General fluid temperature is all protected
Hold more than 36 DEG C), by liquid coil pipe 11, heat release is heated in gas tank processed after these high-temp liquids entrance gas tank 10 processed, then
Outflow gas tank processed is back to water tank 44 and is heated again by the heating source of outside, move in circles, so as to realize holding gas tank processed
Temperature heating of continuing rising.Outside heating source is that the electric heater 41 that connection water tank is heated to it or outside are connect by pipeline
Enter the vapour source 43 of water tank.The vapour source 43 that the connection of the latter's pipeline is accessed can come from the output of burning boiler in practical application
Steam, or from cloth grass cleaning equipment in high-temperature steam washing, drying, plate etc. after operation in the past as Industry Waste row
Steam.Recycling for steam can so be realized.
In gas tank processed 10 by be input into liquid light hydrocarbon mixing forced air in the presence of high temperature physical transformations into high concentration
Gasification lighter hydrocarbons, and connected high concentration gasification lighter hydrocarbons output a to neutralizing tank 50 by pipeline.
The mixed air-conditioning pressure device 70 of the connection of neutralizing tank 50 one, mixed one end of air-conditioning pressure device 70 is connected with gas tank 30 is entered, the other end
Connection neutralizing tank 50 is used to adjust the composition ratio of the gaseous state lighter hydrocarbons with air of air mixture.The mixed air-conditioning pressure device 70 is by
Cause that the gasification lighter hydrocarbons of air mixture and the composition ratio of air are 15-21 in neutralizing tank with input air in tank:85-79.Neutralize
Air mixture in tank 50 connects gas tank 60 and is stored by pipeline.
The pressure of air mixture is dropped to 5-13kpa by gas tank 60 by connecting a dropping valve 80 from 15-30kpa, and is led to
Pipeline final output is crossed to burning boiler.Finally exported again as gas tank required for carrying out burning generation cleaning cloth grass to boiler
Steam.
General principle of the present utility model and principal character and advantage of the present utility model has been shown and described above.One's own profession
The technical staff of industry it should be appreciated that the utility model is not restricted to the described embodiments, described in above-described embodiment and specification
Simply illustrate principle of the present utility model, on the premise of the utility model spirit and scope are not departed from, the utility model is also
Various changes and modifications are had, these changes and improvements are both fallen within the range of claimed the utility model.The utility model
Claimed scope is by appending claims and its equivalent thereof.
Claims (8)
1. it is used to providing the light hydrocarbon system of cleaning cloth grass steam, including gas tank processed, oil tank, enters gas tank, liquid circulation
Heater, neutralizing tank and gas tank;Characterized in that, the oil tank of the liquid light hydrocarbon that is stored with connects gas tank processed by pipeline
Liquid light hydrocarbon is input into it;It is described enter gas tank the forced air that gas tank processed is input into promotion light hydrocarbon to it is connected by pipeline;
The hydronic heater by with gas tank processed build circulation line be connected come liquid that heat energy is carried to its lasting input after
And realization is heated to gas pot liquid processed;By being input into liquid light hydrocarbon in mixing forced air and high temperature in the gas tank processed
In the presence of physical transformations into high concentration gasify lighter hydrocarbons, and by pipeline connect by high concentration gasify lighter hydrocarbons export to one neutralize
Tank;The mixed air-conditioning pressure device of the neutralizing tank connection one, the mixed air-conditioning pressure device causes neutralization by input air in neutralizing tank
The gasification lighter hydrocarbons of in-tank mixing combustion gas are 15-21 with the component ratio of air:85-79;Air mixture in the neutralizing tank is led to
Cross pipeline connection gas tank and to be stored, finally by gas tank, pressure regulation exports and carries out burning to boiler and produce cleaning cloth grass institute again
The steam of needs.
2. the light hydrocarbon system for providing cleaning cloth grass steam according to claim 1, it is characterised in that described
Oil tank is provided with filtering and pressue device.
3. the light hydrocarbon system for providing cleaning cloth grass steam according to claim 1, it is characterised in that described
Oil tank is connected with some for the blow-down pipe to oil tank exhaust step-down.
4. the light hydrocarbon system for providing cleaning cloth grass steam according to claim 1, it is characterised in that described
Enter gas tank to connect air compressor by one end to be input into forced air to gas tank processed.
5. the light hydrocarbon system for providing cleaning cloth grass steam according to claim 1, it is characterised in that described
Hydronic heater includes being connected liquid circulation line, water tank and heating source with gas tank processed, and the heating source is connection water tank
The electric heater or the outside vapour source that access water tank is connected by pipeline heated to it.
6. the light hydrocarbon system for providing cleaning cloth grass steam according to claim 5, it is characterised in that described
Liquid circulation line connection is placed in the liquid coil pipe in gas tank processed.
7. the light hydrocarbon system for providing cleaning cloth grass steam according to claim 1, it is characterised in that described
The pressure of air mixture is dropped to 5-13kpa by gas tank by connecting a dropping valve from 15-30kpa, and finally defeated by pipeline
Go out to burning boiler.
8. the light hydrocarbon system for providing cleaning cloth grass steam according to claim 1, it is characterised in that described
Mixed air-conditioning pressure device one end is connected with gas tank is entered, and other end connection neutralizing tank is used to adjust the gaseous state lighter hydrocarbons and air of air mixture
Composition ratio.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621348276.XU CN206310528U (en) | 2016-12-09 | 2016-12-09 | Light hydrocarbon system for providing cleaning cloth grass steam |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621348276.XU CN206310528U (en) | 2016-12-09 | 2016-12-09 | Light hydrocarbon system for providing cleaning cloth grass steam |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206310528U true CN206310528U (en) | 2017-07-07 |
Family
ID=59250265
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201621348276.XU Expired - Fee Related CN206310528U (en) | 2016-12-09 | 2016-12-09 | Light hydrocarbon system for providing cleaning cloth grass steam |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN206310528U (en) |
-
2016
- 2016-12-09 CN CN201621348276.XU patent/CN206310528U/en not_active Expired - Fee Related
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Date | Code | Title | Description |
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GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170707 Termination date: 20171209 |