CN1193599A - Closed liquid transferring and storing system - Google Patents
Closed liquid transferring and storing system Download PDFInfo
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- CN1193599A CN1193599A CN97101595A CN97101595A CN1193599A CN 1193599 A CN1193599 A CN 1193599A CN 97101595 A CN97101595 A CN 97101595A CN 97101595 A CN97101595 A CN 97101595A CN 1193599 A CN1193599 A CN 1193599A
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Abstract
An enclosed liquid delivering and storing system for oil depot, oiling station, oil refinery, or others for volatile toxic liquid features that it has additional boosting system and recovering and liquefying system for volatile gas, so avoiding interrupted delivering caused by gas resistance or cavitation and environmental pollution caused by volatile gas.
Description
Closed liquid transferring and storing system is applicable to that oil depot, petrol service station, refinery transmitting-receiving store the place and other transmitting-receiving poisonous, volatile liquid stores place installation application.
Retrieve and consult pertinent data according to domestic " Chinese patent Digest data bank " (CD), the present patent of this system not being installed in above place as yet or this system being arranged.The problem that closed liquid transferring and storing system solves is: under existing open liquid transferring and storing system appointed condition, the low level jar produces vapour lock or cavitation erosion in the transmitting-receiving process, causes transfusion to be interrupted; Liquid is the direct exhaust to atmosphere of volatile gas in the transmitting-receiving storage process, causes the waste of liquid charging stock and to the pollution of environment.After this system is installed, can reclaim a large amount of liquid charging stocks, improve environment.Produce considerable economic and environmental benefit.
Closed liquid transferring and storing system is on existing open liquid transferring and storing system (open liquid transferring and storing system is liquid direct exhaust to atmosphere of volatile gas in the transmitting-receiving process) basis, sets up a pressure charging system and Volatile Gas and reclaims liquefaction system.
Closed liquid transferring and storing system is compared with existing open liquid transferring and storing system and is had the following advantages:
1, solved existing open liquid transferring and storing system and when transmitting-receiving, produced vapour lock or cavitation erosion, caused receiving and dispatching the problem that operation is interrupted because of temperature is high.
2, solved liquid charging stock waste that the Volatile Gas exhaust to atmosphere caused and to the pollution of environment.According to statistics, under existing open liquid transferring and storing system condition, receive and dispatch storaging liquid, the petrol service station that year transmitting-receiving is 5000 tons, year air loss is 5 to 10 tons, the oil depot year air loss of one 20000 cubic meter is 50 to 100 tons.Non-conservation tank air loss is bigger.Cause aerial contamination behind the direct exhaust to atmosphere of these volatilization gas, influence the healthy of operating personnel and resident.Adopt closed liquid transferring and storing system the volatile gas of these losses can be reclaimed liquefaction and utilize again, save a large amount of fluid supply material.Improve working environment, improved the degree of safety in transmitting-receiving storage place.So, adopt closed liquid transferring and storing system can bring considerable economic, environmental benefit and social benefit.
3, closed liquid transferring and storing system has comformability and the property transformed widely.Its comformability be can be widely used in that all are poisonous, the transmitting-receiving of effumability liquid stores the place.As: places such as petrol service station, oil depot.Its property transformed is meant: only need existing tank car, the gun barrel that refuels are transformed a little, set up small number of devices and can realize on the basis of existing open liquid transferring and storing system.Can obtain bigger income with less input.
With reference to Fig. 1, closed liquid transferring and storing system is formed: native system can be considered by three big subsystems to be formed, that is: liquid transferring and storing system, pressure charging system, Volatile Gas reclaim liquefaction system.(among Fig. 1, liquid conducting pipes that solid line is designated as, dotted line are designated as the Volatile Gas return, long and short dash line is designated as pressure letter shoot road)
Liquid transferring and storing system: by by-pass valve control (3), (4), (5), (6), (7), (8), (9), (10), (11), (12), (13), (14), (15), (16), (17), (18), (19), (20), (21), (22), (23), (24), (25), (26), (27), (28), (29), oil transportation road (30), (31), (32), (33), (34), (35), (36), (37), (AA '), (BB '), (CC '), solid lines such as (EE ') is marked, oil filling riser (38), liquid storage container (39), (40), (41), (42), (43), (44) form.
Pressure charging system: by air compressor (45), head tank (46), by-pass valve control (47), (48), (49), (50), (51), (52), compositions that long and short dash line is marked such as pressure letter shoot road (53), (54), (55), (56), pressure safety valve (PSV) (90).
Volatile Gas reclaims liquefaction system: by Volatile Gas liquefier (the 57) (patent equipment of available Xinkai Universal Testing Factory, Xicheng District, Beijing: a kind of gas exhausting and light-oil recovering device for oil tank.Patent announcement number=CN-210131U), liquefier holding vessel (58), dotted lines such as Volatile Gas return (59), (60), (61), (62), (63), (64), (65), (66), (67), (68), (69), (70), (71), (72), (73), (74) are marked, by-pass valve control (75), (76), (77), (78), (79), (92), vent valve (80), (81), (82), (83), (91), (95) are unified into table (84), (85), (86), (87), (88), (89).
Working process is:
Under static storage condition: when the gas that evaporates in the holding vessel was breathed under action of thermal difference, big corrugated hose by-pass valve control (77), (78), (79) were closed.When outside exhalation Volatile Gas, holding vessel (42) or (43) or (44) interior Volatile Gas are breathed out through vent valve (81) or (82) or (80), enter little breathing circuit pipeline (64) or (67) or (72) → (74) → (69) or → Volatile Gas liquefier (57) liquefaction back → liquefier holding vessel (58) → valve (13) → (15) → depositing tank (44), or back residual gas → vent valve (83) → exhaust to atmosphere of liquefaction.
Its gas return path is when in the outside air suction tank: air → vent valve (83) → (58) → (70) → (57) → (69) → (74) or → (73) → (72) → (80) → (44), or → (67) → (82) → (43), or → (64) → (81) → (42).
In working order down: when liquid in the tank car (39) is imported holding vessel (43) or (42), can not produce vapour lock or cavitation erosion and cause receiving under the situation that liquid interrupts if temperature is low, job procedure is: the pressure charging system starting, air compressor (45) starts, and produces pressure in air → vent valve (83) or volatilization gas → (58) → Open valve (47) → air compressor (45) → Open valve (48) → head tank (46) → Open valve (49) → pipeline (54) → Open valve (52) → (55) → (56) → tank car vent valve (91) → (39).The interior liquid of tank car is through tank car emptying short tube (148) → oil filling riser (38) → Open valve (20) → oil pipeline (30), (31) → Open valve (4) → Open valve (8) → starting infusion pump (1) → Open valve (9) → Open valve (18) or (17) → BB ' or AA ' → Open valve (27) or (24) → (28) or (25) → fluid reservoir (43) or (42) under pressure.
The working process in Volatile Gas loop is: when temperature high and produce vapour lock or cavitation erosion when causing receiving oil and interrupting, behind the liquid input holding vessel (42) or (43), Volatile Gas prevents the transfusion interruption through vent valve (81) or (82) → big breathing circuit pipeline (63) or (66) → Open valve (77) or (78) → volatilizer loop pipe (65) or (68) → (74) → (69) → (57) → (70) → (58) → (47) → (45) → (48) → (46) → (49) → (54) → (52) → (56) → (91) → (39) continuation pressurization.Can not produce vapour lock or when cavitation erosion when temperature is high, then the infusion pump starting enter normal after, pressure charging system quits work.Liquid gas exchanges between holding vessel (42) or (43) and tank car (39), and promptly the Volatile Gas of discharging in (42) or (43) enters tank car (39) or enters liquefaction in the Volatile Gas liquefier (57) through the Volatile Gas circuit system.Its loop is: discharge in (42) or (43) gas → (81) or (82) → big breathing circuit pipe (63) or (66) → Open valve (77) or (78) → Volatile Gas return (65) or (68) → (74) or → Open valve (92) → (56) → (91) → (39), or → (69) → (57) → (70) → (58) → (83) → atmosphere.It is identical to send to tank car (39) Volatile Gas principle of reciprocity from (42) or (43).Liquid gas between each jar exchanges also principle herewith.
When sending to filling opening in the holding vessel (42) and send, liquid flow is: (42) interior liquid gravity flow → Open valves (25) → Open valve (24) → liquid-transport pipe-line (E ' E) or → Open valve (22) → liquid feeding oil filling riser (163) → transportation tank oil-feed short tube (93) → transportation tank (40), or → Open valve (23) → (37) → liquid feeding rifle (94) → molten device of dress liquid (41) in.Volatile Gas flows to: discharge gas → automobile vent valve (95) → Volatile Gas return (62) → Open valve (76) → Volatile Gas reflux line (61) → (74) → (65) → Open valve (77) → (63) → (42) in (40), discharge gas → liquid feeding rifle air gate (59) → Open valve (75) → (60) → (61) → (74) → (65) → Open valve (77) → (63) → (42) in (41).
Said system is tank car and trestle to be arranged or the use flow setting of transmitting-receiving storage vault of transmitting-receiving harbour is arranged.In the area or the place that can not cause producing vapour lock or cavitation erosion, the pressure charging system of this system can not be provided with.
With this system applies when the petrol service station.
With reference to Fig. 2, be the setting of a kind of oil product of petrol service station of imagination.Equipment has: fuel charger (96), oil container (oil drum or fuel tank etc.) (97), petrol storage tank (98), (99), transmitting-receiving pump (101) carries out closed defeated storage system with these installations and facilities and installs, flow process such as Fig. 2, this flow process only designs liquid transferring and storing system and volatilizer reclaims liquefaction system.
Liquid transferring and storing system: by fuel charger (96), oil vessel (97), (98), (99), (100), solid lines such as delivery line (102), (103), (AA '), (BB '), (CC '), (EE '), (E ' E ' ') are marked, fuel transfer pump (101), nozzle (104), by-pass valve control (105), (106), (107), (108), (109) (110), (111), (112), (113), (114), (115), (116), (117), (118), (119), (120) are formed.
Volatilizer reclaims liquefaction system: by Volatile Gas liquefier holding vessel (121), Volatile Gas liquefier (122), dotted lines such as Volatile Gas return (123), (124), (125), (126), (127), (128), (129), (130), (131), (132), (133), (134) are marked, by-pass valve control (135), (136), (137), (138), vent valve (139), (140), (141), (142) are unified into table (143), (144), (145), (146), (147) composition.
Working process:
Under static storing state, holding vessel (98), (99) interior oil vapour general breathing under action of thermal difference, at this moment, valve (135), (136), (137), (138) are closed, when oil vapour was breathed out, (98) or (99) interior oil vapour → vent valves (141) or (140) → Volatile Gas return (130) or (129) → (133) → Volatile Gas liquefier (122) → (121) → on a small quantity remained Volatile Gas through vent valve (142) exhaust to atmosphere.When in air admission holding vessel (98) or (99), flow process is: air → vent valve (142) → (121) → (122) → (133) or → (130) → (141) → (98), or → (126) → (129) → (140) → (99).When oil product in (98) is issued user's container (97), its working process is that oil product flows to: (98) interior oil product → Open valve (116) → Open valve (115) → Open valve (114) → oil pipeline (EE ') → fuel charger (96) → transport pipe (103) → nozzle (104) → container (97).Oil vapour flows to: (97) interior oil vapour → nozzle air gate (134) → Open valve (135) → Volatile Gas counter flow pipe (126) or → (131) → Open valve (138) → (132) → vent valve (141) → (98), or → (133) → (122) → (121) → (142) → atmosphere.
When oil product came oil to deposit (99) in the transportation tank (100), oil product flowed to and is: and (100) interior oil product → Open valve (113) → oil pipeline (C ' C) → Open valve (109) → Open valve (106) → startup fuel transfer pump (101) → Open valve (105) → delivery line (102) → Open valve (110) → oil pipeline (AA ') → Open valve (118) → Open valve (119) → holding vessel (99).Oil vapour flows to and to be: (99) interior oil vapour → vent valve (140) → Volatile Gas return (128) → Open valve (137) → (127) or → Volatile Gas return (125) → Open valve (136) → (124) → transportation tank vent valve (139) → transportation tank (100), or → back residual gas → (121) → vent valve (the 142) → exhaust to atmosphere of Volatile Gas return (126) → (133) → Volatile Gas liquefier (122) liquefaction.
Reason herewith mutually between all the other jars and the jar.
Other can be looked particular case and transform and install according to the principle of closed liquid transferring and storing system in different places.
The equipment of the required transformation of closed liquid transferring and storing system:
One, tank car
With reference to Fig. 3, partly be on the basis of original tank car to the transformation of tank car, set up the liquid in-out short tube (148) that is fixed in the tank car; Take out end liquid short tube (149); Vent valve (151) is transformed into and revolves outspoken fast bonded assembly vent valve; Hand-hole (150) adds the tightening seal washer sealing; Transmitting-receiving liquid short tube flap (153), (152).
Effect is: short tube junction (155) are adopted and to be revolved outspoken speed and connect to mark with Fig. 1 and receive and dispatch oil filling riser communication port (164) and be complementary and be connected, (154) marking the communication port (165) of receiving end oil pipes (34) with Fig. 1 is complementary and is connected, the communication port (156) of vent valve (151) adopts and revolves outspoken speed connects with Fig. 1 marks trestle Volatile Gas loop pipe (56) communication port (157) and be complementary and be connected, (153), (152) use in transportation, plays sternly to seal the short tube mouth.Improved like this tank car can be realized the sealing transmitting-receiving.
Two, transportation tank
With reference to Fig. 4, partly be on the basis of original transportation tank to the transformation of transportation tank, set up oil-feed short tube (157), the ventilation mouth (161) of transforming vent valve (160) is for revolving outspoken speed connection, oil-feed short tube flap (158).
Effect is: oil-feed short tube communication port (162) adopts and to revolve outspoken speed and connect to mark with Fig. 1 and add oil crane tube communication port (163) and be complementary and be connected, vent valve communication port (161) and Fig. 1 mark the communication port (166) of Volatile Gas loop flexible pipe (62) or communication port (167) that Fig. 2 marks Volatile Gas loop flexible pipe (124) and are complementary and are connected, and oil-feed short tube lid (158) plays tight envelope effect in transit.Hand-hole (159) adds the effect that tightening seal washer has sealed the sealing hand-hole.
Three, railway transceiver station oil filling riser
With reference to Fig. 5, adopt the moving universal oil filling riser of tooth, its structure is: by deflector (168), (169), (170), (171); rocking arm quadrant gear (172); driven wheel (173), handle rocking arm (174), tiltedly straight tube (175); cantalever tube (176); adaptor union (164), set pin (177), Connection Card (178); bearing support (179), adaptor union communication port connection pipe (180).
Principle of work: under the effect of deflector (168), (169), (170), (171), oil filling riser communication port (164) can turn round arbitrarily at vertical surface and horizontal surface; when rocker handle (174) drives driven wheel (173) rotation; rocking arm quadrant gear (172) rotates, and cantalever tube (176) is turned round up and down.Adaptor union Connection Card (178) is complementary with turnover shown in Figure 3 oil short tube communication port (155) and is connected, or is complementary with transportation tank oil-feed short tube communication port (162) shown in Figure 4 and is connected.
Four, nozzle
With reference to Fig. 6, fuel-displaced short tube to existing nozzle is transformed into the fuel-displaced short tube of the double hole channel that has air gate, its structure is: by endoporus (181), and outer hole (182), inner hole wall (183), outer hole wall (184), seal boss (185), tightening seal washer (186), oil outlet connects boss (187), air gate (188), air extractor duct connects boss (189).
Use the place: when interior the liquid feeding of small container ((41) as shown in Figure 1, (97) shown in Figure 2), this nozzle of palpus.
Principle of work: when liquid filled container (41) that the insertion of liquid feeding rifle liquid feeding short tube is shown in Figure 1 or liquid filled container (97) shown in Figure 2, fuel-displaced short tube seal boss (185), the inlet of tightening seal washer (186) and liquid filled container shown in Figure 2 (97) or (41) shown in Figure 1 is adjacent to, when liquid when endoporus (181) injects (97) shown in Figure 2 or (41) shown in Figure 1, (97) or (41) in gas through outer hole (182) to air gate (188), air extractor duct connects boss (189) and is connected with Volatile Gas loop pipe (59) shown in Figure 1 or Volatile Gas loop pipe (134) shown in Figure 2, makes Volatile Gas enter Volatile Gas recovery liquefaction system.
Five, vent valve
With reference to Fig. 7, vent valve adopts the blue dish of valve interconnection system, communication port (190) is connected with big breathing Volatile Gas return (63) or (66) or (71) shown in Figure 1, be connected with big breathing Volatile Gas loop pipe (132) or (128) shown in Figure 2, communication port (191) is connected with forcer delivery duct (203) shown in Figure 1, communication port (192) is connected with the little breathing circuit pipe of Volatile Gas (64) or (67) or (72) shown in Figure 1, is connected with the little breathing circuit pipeline of Volatile Gas (130) or (129) shown in Figure 2.
Six, with reference to Fig. 8, substitute transceiver, under the situation that tank car and transportation tank are not transformed, use.
Its structure is: by round sealed lid (193), pass in and out oily short tube (194), tightening seal washer (195), pass in and out oily short tube communication port (196), Volatile Gas air gate communication port (198), Volatile Gas air gate (197), hold down groove (199), (200), (201), (202).
Principle of work:
Place as shown in Figure 1 hand-hole (150) or transportation tank hand-hole (204) or transportation tank hand-hole (205) shown in Figure 2 to locate this alternative transceiver, the sealing hand-hole, communication port (196) is complementary with the communication port (163) of railway oil filling riser communication port (164) shown in Figure 1 or automobile fuel filler oil filling riser and is connected, and the communication port (167) of the communication port (166) of Volatile Gas outlet (198) and Volatile Gas loop flexible pipe (56) communication port (157) shown in Figure 1, Volatile Gas loop flexible pipe (62) shown in Figure 1, Volatile Gas flexible pipe (124) shown in Figure 2 is complementary and is connected.Be implemented in the sealing transmitting-receiving under tank car and the not transformation condition of transportation tank.
More than explanation is the principle of this system, and the mounting means that it is concrete and the set-up mode of reforming equipment, material use and size can be determined in specific implementation process.This explanation only is illustrated its principle.
The diagram of scrap build also is a principle schematic, and concrete size, materials used are determined in concrete enforcement.
Claims (18)
1 with reference to Fig. 1, closed liquid transferring and storing system, and this system sets up pressure charging system and Volatile Gas recovery liquefaction system on the basis of the equipment setting in existing oil depot, petrol service station, refinery transmitting-receiving storage area, highly volatile all kinds of other liquid transmitting-receiving storage places.It is characterized in that:
1. described pressure charging system: be by air compressor (45), head tank (46), by-pass valve control (47), (48), (49), (50), (51), (52), shown in the long and short dash lines such as pressure letter shoot road (53), (54), (55), (56), pressure safety valve (PSV) (90) is formed.
2. described Volatile Gas reclaims liquefaction system: be by Volatile Gas liquefier (57), liquefier holding vessel (58), shown in the dotted lines such as Volatile Gas return (59), (60), (61), (62), (63), (64), (65), (66), (67), (68), (69), (70), (71), (72), (73), (74), by-pass valve control (75), (76), (77), (78), (79), (92), vent valve (80), (81), (82), (83) are unified into table (84), (85), (86), (87), (88), (89) composition.
2, according to claim 1 described system, it is characterized in that: when the liquid in suction tank car (39) or the low level jar (44), when the starting stage produces vapour lock or cavitation erosion, Air compressor (45) starting, produce pressed gas charged pressure jar (46), head tank (46) internal pressure gas charges into pressed gas in the tank car (39) or generation malleation in the low level jar (44) through excess pressure letter shoot road, by-pass valve control.
3, according to claim 1 described system, it is characterized in that: all liquid storage containers: (39) among Fig. 1 or (40) or (41) or (42) or (43) or (44) are in transmitting-receiving or storage process, volatile gas is through vent valve (91) or (95) or nozzle air gate (59) or (81) or (82) or (80), link to each other with Volatile Gas loop pipe (74) through control cock (92) or (76) or (75) or (77) or (78) or (79), Volatile Gas loop effuser (74) links to each other with Volatile Gas liquefier (57) admission port, air extractor duct is connected with low-voltage safety jar (58), and low-voltage safety jar (58) installation security ventilating valve (83) (than the control presssure height of holding vessel vent valve) communicates with atmosphere or is connected with Air compressor (45) import; Volatile gas is exchanged between each liquid storage container (39) or (40) or (41) or (42) or (43) or (44) or enter Volatile Gas liquefier (57) liquefaction and reclaim the back residual gas and enter low pressure jar (58), the interior gas of low pressure jar (58) or continue to enter the recycle of air compressor air intake mouth or directly through security ventilating valve (83) exhaust to atmosphere.
4, according to the described device of claim 3, it is characterized in that: the little breathing circuit arm of vent valve direct connection Volatile Gas (64) of fluid reservoir (42) or (43) or (44) or (67) or (72), the little breathing circuit arm of Volatile Gas (64) or (67) or (72) directly are connected with Volatile Gas loop effuser (74), open when the transmitting-receiving operation by-pass valve control (77) or (78) or (79), closes at ordinary times.
5, according to claim 3, it is characterized in that: the control presssure of fluid reservoir vent valve (81) or (82) or (80) must be gone up the control presssure of security ventilating valve (83) less than low pressure jar (58), and both the action of fluid reservoir vent valve must be prior to low pressure jar safety valve (83).
6, according to claim 1,2,3,4,5, it is characterized in that: utilize native system or native system equipment component or by of the installation of its principle in practical application area.
7, with reference to Fig. 3, the annex of tank car is set up, and it is characterized in that: set up transmitting-receiving liquid short tube (148), take out end short tube (149) and be fixed on the tank car, vent valve repacks rotary quick connection vent valve (151) into.
8, according to claim 7, it is characterized in that: transmitting-receiving liquid short tube communication port (155), take out end liquid short tube communication port (154), vent valve communication port (156) is rotary quick connection, when oil transmitting-receiving and oil filling riser or take out bottom tube or Volatile Gas backflow arm is connected.With rotary lid (153), (152) short tube communication port (154), (155) are sealed in the transportation.
9, with reference to Fig. 4, the annex of transportation tank is set up, and it is characterized in that: oil-feed short tube (157) is fixed in the tank car, and vent valve is used rotary connection vent valve (160) instead.
10, according to claim 9, it is characterized in that: oil-feed short tube communication port, vent valve communication port are rotary quick connection, are connected with hair oil oil filling riser or Volatile Gas backflow arm when adorning liquid in tank car.Oil-feed short tube mouth seals the short tube mouth with rotary lid (158) in the transportation.
11, with reference to Fig. 5, tooth moves universal oil filling riser, it is characterized in that: by deflector (168), (169), (170), (171), oblique straight tube (175), cantalever tube (176), driven wheel (173), rocking arm quadrant gear (172), handle rocking arm (174), rotary Quick Connect Kit compositions such as (164).
12, according to claim 11, it is characterized in that: cantalever tube (176) is solidified as a whole with rocking arm quadrant gear (172), handle rocking arm (174) is solidified as a whole with driven wheel (173), handle rocking arm (174) drives driven wheel (173) rotation, driven wheel (173) drives rocking arm quadrant gear (172) rotation, makes cantalever tube rotation up-and-down movement.
13, according to claim 11, it is characterized in that: oil inlet and outlet (164) is used rotary Quick Connect Kit.
14, with reference to Fig. 6, the fuel-displaced short tube of nozzle double hole channel is characterized in that: by a concentric double hole channel endoporus (181) and outer hole (182), volatile gas deflation hole (188), boss compositions such as (185).
15 according to claim 14, it is characterized in that: inner duct (181) links to each other with nozzle, outer duct (182) fuses with deflation hole (188), deflation hole (188) is connected with Volatile Gas loop arm, one step (185) and a seal ring (186) are arranged on the outer tube wall, hand nozzle sealing liquid filled container mouth makes Volatile Gas discharge from deflation hole (188) during oiling.
16, with reference to Fig. 8, substitute transceiver, it is characterized in that: by rotary quick connection liquid in-out short tube (194), Volatile Gas breather hole (197), communication port (198), disk cover (193) is formed.
17, according to claim 16, it is characterized in that: do not set up under the situation of annex at tank car or transportation tank, place tank car or transportation tank hand-hole place sealing hand-hole, realize the sealing transmitting-receiving.
18, according to claim 7,8,9,10,11,12,13,14,15,16,17, it is characterized in that: above reforming equipment is carried out patent transformation or production and processing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN97101595A CN1193599A (en) | 1997-03-17 | 1997-03-17 | Closed liquid transferring and storing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN97101595A CN1193599A (en) | 1997-03-17 | 1997-03-17 | Closed liquid transferring and storing system |
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| Publication Number | Publication Date |
|---|---|
| CN1193599A true CN1193599A (en) | 1998-09-23 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN97101595A Pending CN1193599A (en) | 1997-03-17 | 1997-03-17 | Closed liquid transferring and storing system |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103159159A (en) * | 2011-12-18 | 2013-06-19 | 沈阳黎明航空发动机(集团)有限责任公司 | Storing and precipitating process of jet fuel |
| CN103738907A (en) * | 2014-01-15 | 2014-04-23 | 杨江山 | Oil vapor recovery atomizer |
| CN104261150A (en) * | 2014-08-22 | 2015-01-07 | 安徽淮化股份有限公司 | Discharging system for ammonium nitrate tank truck |
| CN108910320A (en) * | 2018-05-26 | 2018-11-30 | 永春科盛机械技术开发有限公司 | A kind of volatile liquid storage device |
-
1997
- 1997-03-17 CN CN97101595A patent/CN1193599A/en active Pending
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103159159A (en) * | 2011-12-18 | 2013-06-19 | 沈阳黎明航空发动机(集团)有限责任公司 | Storing and precipitating process of jet fuel |
| CN103159159B (en) * | 2011-12-18 | 2015-10-28 | 沈阳黎明航空发动机(集团)有限责任公司 | A kind of storage depositing technology of jet fuel |
| CN103738907A (en) * | 2014-01-15 | 2014-04-23 | 杨江山 | Oil vapor recovery atomizer |
| CN103738907B (en) * | 2014-01-15 | 2016-06-08 | 福建省东方瑞迩机器制造有限公司 | Oil vapor recovery atomizer |
| CN104261150A (en) * | 2014-08-22 | 2015-01-07 | 安徽淮化股份有限公司 | Discharging system for ammonium nitrate tank truck |
| CN104261150B (en) * | 2014-08-22 | 2017-08-25 | 安徽淮化股份有限公司 | Discharge system for ammonium nitrate tank car |
| CN108910320A (en) * | 2018-05-26 | 2018-11-30 | 永春科盛机械技术开发有限公司 | A kind of volatile liquid storage device |
| CN108910320B (en) * | 2018-05-26 | 2020-08-25 | 华融化学股份有限公司 | Volatile liquid storage device |
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