US4233137A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of heat recovering from high temperature thermally cracked hydrocarbons
Assignee: Kureha Corp
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Filing: 1979-03-30
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Granted: 1980-11-11
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Expires: 1999-03-30
Abstract
Abstract A method for recovering sensible heat from a thermally decomposed high temperature hydrocarbon gas product in the form of high pressure steam of from 40 to 100 kg/cm2 has been discovered. This method comprises pre-cooling at first the thermally decomposed gas product of high temperature by mixing said gas product with sprayed low temperature hydrocarbon oil as a quenching oil to a temperature of about 300 DEG to 400 DEG C.; and then passing the mixture through the tubes of a shell-and-tube type heat exchanger so as to transfer the heat of said resulting mixture into a high pressure water flowing through the space of the shell side thereof to recover a high pressure steam, followed by separating the condensed hydrocarbon oil from the mixture to reuse said oil by recirculation.
Inventors
- 👤 Kiyoji Ozaki
- 👤 Akinobu Fukuhara
- 👤 Takuji Hosoi
- 👤 Yasuo Sagi
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 09:28
CPC Classifications
C; C10; C10G; C10G9/00; C10G9/002; C10J; C10J3/00; C10J3/46; C10J3/48; C10J3/52; C10J3/526; C10J3/72; C10J3/82; C10J3/84; C10J3/86; C10K; C10K1/00; C10K1/08; C10K1/16; C10K1/18; C10G2400/00; C10G2400/20; C10J2300/00; C10J2300/16; C10J2300/1687; C10J2300/18; C10J2300/1861; C10J2300/1884; C10J2300/1892; Y; Y02; Y02P; Y02P20/00; Y02P20/10; Y02P20/129; Y10; Y10S; Y10S585/00; Y10S585/949; Y10S585/95
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
244 words
A method of recovering heat from a high temperature gas product obtained by thermal decomposition of hydrocarbons in the form of high pressure steam which comprises (a) precooling, in a vessel comprising a precooling zone, a heat exchange zone and a separating zone, the high temperature gas product in the precooling zone by mixing said gas product with a sprayed low temperature hydrocarbon oil of a by-product obtained from said thermal decomposition of hydrocarbons, which contains from 30 to 80 percent by weight of a pitch based on the weight of said sprayed low temperature hydrocarbon oil, as a quench to a temperature of from 300° C. to 400° C.; (b) passing the resulting mixture downwardly from the precooling zone through the tubes of a substantially vertical shell-and-tube type heat exchange means, at a linear gas velocity of 15 to 50 meters per second in said tubes to form a thin liquid film layer of the sprayed oil on the inside walls thereof, and transferring the heat contained in said resulting mixture into a high pressure water flowing through the shell side of the heat exchange means and recovering therefrom a high pressure steam of from 40 to 100 kg/cm 2 ; (c) separating the said hydrocarbon oil in the separating zone from said resulting mixture passed through the tubes of said heat exchange means downwardly to the separating zone; and (d) recirculating the separated hydrocarbon oil as a quench to the precooling zone.
Claim 2
Independent Claim
244 words
A method of recovering heat from a high temperature gas product obtained by thermal decomposition of hydrocarbons in the form of high pressure steam which comprises (a) precooling, in a vessel comprising a precooling zone, a heat exchange zone and a separating zone, the high temperature gas product in the precooling zone by mixing said gas product with a sprayed low temperature hydrocarbon oil of a by-product obtained from said thermal decomposition of hydrocarbons, which contains from 30 to 80 percent by weight of a pitch based on the weight of said sprayed low temperature hydrocarbon oil, as a quench to a temperature of from 300° C. to 400° C.; (b) passing the resulting mixture downwardly from the precooling zone through the tubes of a substantially vertical shell-and-tube type heat exchange means, at a linear gas velocity of 15 to 50 meters per second in said tubes to form a thin liquid film layer of the sprayed oil on the inside walls thereof, and transferring the heat contained in said resulting mixture into a high pressure water flowing through the shell side of the heat exchange means and recovering therefrom a high pressure steam of from 40 to 100 kg/cm 2 ; (c) separating the said hydrocarbon oil in the separating zone from said resulting mixture passed through the tubes of said heat exchange means downwardly to the separating zone; and (d) recirculating the separated hydrocarbon oil as a quench to the precooling zone.
Claim 3
Dependent Claim
30 words
The method of claim 1, wherein the high temperature gas product is obtained by cracking a material selected from the group consisting of naphtha, gas oil, crude oil and residue.
Claim 4
Dependent Claim
21 words
The method of claim 1, wherein the high temperature gas product is obtained by carbonization, hydrocarbonization, gasification or hydrogasification of coal.
Claim 5
Dependent Claim
22 words
The method of claim 1, wherein a portion of the quench is flowed downwardly along the inside wall of the precooling zone.
Claim 6
Dependent Claim
17 words
The method of claim 1, wherein steam at above 150° C. is passed into the precooling zone.
Claim 7
Dependent Claim
30 words
The method of claim 1, wherein steam at above 150° C. and a portion of the quench are passed into and downwardly along the inside wall of the precooling zone.
Claim 8
Dependent Claim
23 words
The method of claim 1, wherein the inlet temperature of the quench is in the range of from 250° C. to 350° C.
Claim 9
Dependent Claim
26 words
The method of claim 1, wherein the inlet temperature of the high temperature gas product is in the range of from 450° C. to 1400° C.
Claim 10
Dependent Claim
18 words
The method of claim 1, wherein said linear gas velocity is between 20 and 50 meters per second.
Claim 11
Independent Claim
239 words
A method of recovering heat from a high temperature gas product obtained by thermal decomposition of hydrocarbons in the form of high pressure steam in a vertical vessel comprising downwardly a precooling zone, a heat exchange zone and a separating zone, which comprises the steps of (a) precooling the high temperature gas product in the precooling zone by mixing said gas product with a sprayed low temperature hydrocarbon oil, which contains from 30 to 80 percent by weight of a pitch based on the weight of said sprayed low temperature hydrocarbon oil, as a quench to a temperature of from 300° C. to 400° C.; (b) passing the resulting mixture downwardly from the precooling zone through the tubes of a vertical shell-and-tube type heat exchange means at a linear gas velocity of from 15 to 50 meters per second in said tubes to form a thin liquid film layer of the sprayed oil on the inside walls thereof, and transferring the heat contained in said resulting mixture into a high pressure water flowing through the shell side of the heat exchange means to recover therefrom a high pressure steam of from 40 to 100 kg/cm 2 ; (c) separating the said hydrocarbon oil in the separation zone from said resulting mixture passed through the tubes of said heat exchange means downwardly to the separating zone; and (d) recirculating the separated hydrocarbon oil as a quench to the precooling zone.
Claim 12
Independent Claim
239 words
A method of recovering heat from a high temperature gas product obtained by thermal decomposition of hydrocarbons in the form of high pressure steam in a vertical vessel comprising downwardly a precooling zone, a heat exchange zone and a separating zone, which comprises the steps of (a) precooling the high temperature gas product in the precooling zone by mixing said gas product with a sprayed low temperature hydrocarbon oil, which contains from 30 to 80 percent by weight of a pitch based on the weight of said sprayed low temperature hydrocarbon oil, as a quench to a temperature of from 300° C. to 400° C.; (b) passing the resulting mixture downwardly from the precooling zone through the tubes of a vertical shell-and-tube type heat exchange means at a linear gas velocity of from 15 to 50 meters per second in said tubes to form a thin liquid film layer of the sprayed oil on the inside walls thereof, and transferring the heat contained in said resulting mixture into a high pressure water flowing through the shell side of the heat exchange means to recover therefrom a high pressure steam of from 40 to 100 kg/cm 2 ; (c) separating the said hydrocarbon oil in the separation zone from said resulting mixture passed through the tubes of said heat exchange means downwardly to the separating zone; and (d) recirculating the separated hydrocarbon oil as a quench to the precooling zone.
Claim 13
Dependent Claim
110 words
The method of claim 10, wherein the high temperature gas product is obtained by cracking gas oil or crude oil; a portion of the quench is flowed downwardly along the inside wall of the precooling zone; steam at about 150° C. and a portion of the quench are passed into and downwardly along the inside wall of the precooling zone; the inlet temperature of the quench is in the range of from 250° C. to 350° C.; the inlet temperature of the high temperature gas product is in the range of from 450° C. to 1400° C.; and said linear gas velocity is between 20 and 50 meters per second.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1983-11-11 | 1984-05-12 | 1984-11-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-11-11 | 1988-05-12 | 1988-11-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-11-11 | 1992-05-12 | 1992-11-11 | $7700.00 | Window Closed / Lapsed |